opstat

CY05 Paradise Fossil Plant (PAF) Plant Operating Statistics Report*

Parameter Unit 01 Unit 02 Unit 03 Unit 1_2 Unit 3_3 Unit 1_3

Average Hourly Gross Load (MW) 646 640 840 643 840 695

Gross Generation (MWh) 4,776,620 5,410,408 4,794,528 10,187,028 4,794,528 14,981,556

Total Station Use (MWh) 367,536 349,920 290,056 717,456 290,056 1,007,512

Net Generation (MWh) 4,409,084 5,060,488 4,504,472 9,469,572 4,504,472 13,974,044

Total Station Use Percent (percent) 7.69 6.47 6.05 7.04 6.05 6.73

Capacity Factor (percent) 77.5 87.7 47.6 82.6 47.6 66.9

Hours of Use (hours) 7397 8452 5,705 15848 5705 21,553

Number of Turbine Startups (No.) 12 4 13 16 13 29

Number of Cold Startups (No.) 6 4 10 10 10 20

Gross Heat Rate (Btu/kWh) 8976 9062 9,872 9024 9,877 9297

Net Heat Rate with Oil (Btu/kWh) 9,724 9,689 10,507 9,708 10,513 9,967

Net Heat Rate without Oil (Btu/kWh) 9,724 9,689 10,507 9,705 10,507 9,964

Boiler Efficiency (percent) 88.7 89.1 85.9 88.9 85.9

Moisture in Fuel Boiler Loss (percent) 1.19 1.25 3.21 1.22 3.21

Hydrogen Loss (percent) 3.87 3.83 4.15 3.85 4.15

Dry Gas Loss (percent) 5.83 5.37 5.36 5.59 5.36

Combustibles in Fly Ash Loss (percent) 0.038 0.057 0.102 0.048 0.102

Fixed Losses (percent) 0.4 0.4 1.3 0.4 1.3

Total Boiler Losses (percent) 11.3 10.9 14.1 11.1 14.1

Throttle Pressure (psig) 2392 2397 3475 2395 3475

Throttle Temperature (deg F) 1050 1050 988.8 1050 988.8

Reheat Temperature (deg F) 990.3 985.5 965.2 987.7 965.2

Condenser Back Pressure (in. Hg) 2.16 2.50 2.75 2.34 2.75

CCW Inlet Temperature (deg F) 67.2 69.3 80.8 68.3 80.8

Air Preheater Air Entering Temp (deg F) 157.4 161.7 110.6 159.7 110.6

Exit Gas Temperature (deg F) 295.9 299.0 307.7 297.6 307.7

Dry Gas Loss Temperature (deg F) 78.7 78.7 97.5 78.7 97.5

Throttle/Feedwater flow (Klb) 33,658,709 38,644,519 ######## 72,303,228 ######## 109,153,019

Superheat Attemperation (percent) 0.022 0.012 0 0.017 0 0.011

Reheat Attemperation (percent) 0.086 0.091 0.801 0.088 0.801 0.329

Makeup Water % (percent) 0.927 1.233 1.21 1.091 1.21 1.131

Building Heating Steam % (percent) 0.000 0.001 0 0.031 0 0.021

Total Air (percent) 122.0 121.2 121.6 121.5 121.6

Total Air at Air Heater Outlet (percent) 143.0 131.2 126.8 136.6 126.8

Coal Burn (Klb) 3,732,920 4,255,235 5,138,936 7,988,155 5,138,936 13,127,091

Combustibles in Fly Ash (percent) 1.72 2.58 4.53 2.20 4.53 3.11

Moisture in Coal, As Fired (percent) 11.9 12.5 25.5 12.2 25.5 17.4

Volatile Matter in Coal, As Received (percent) 34.2 34.4 31.4 34.3 31.4 33.2

Fixed Carbon in Coal, As Received (percent) 45.4 44.5 36.3 44.9 36.3 41.6

Ash Content of Coal, As Received (percent) 8.54 8.57 6.83 8.56 6.83 7.88

Coal Heating Value, As Received (Btu/lb) 11,486 11,522 9,210 11,505 9,210 10,607

Sulfur in Coal, As Received (percent) 2.69 2.69 1.06 2.69 1.06 2.05

Oil Fired (gal.) 134,967 44,989 178,967 179,956 178,967 358,923

Oil Fired Heating Value (Btu/gal.) 138,500 138,500 138,500 138,500 138,500 138,500

Oil Fired Sulfur Content (percent) 0.20 0.20 0.20 0.20 0.20 0.20

PRB Coal Burn, tons/yr** 18,585 29,139 1,834,221 47,724 1,834,221 1,881,945

IL Basin Coal Burn, tons/yr** 1,847,875 2,091,644 734,726 3,939,519 734,726 4,674,245

Total Coal Burn, tons/yr 1,866,460 2,120,783 2,568,947 3,987,243 2,568,947 6,556,190

Percent difference, (1-coalstats/opstats)*100 0.00 0.32 0.02 0.17 0.02 0.11

*Reference: DataFuser output 01/23/06 (Plant 12MTD Operating Statistics Report at PAF for December 2005)

 (Excel file "CY05 Operating Statistics from DataFuser (012306).xls" in FPG Env Affr - TRI folder on "Chapgfs5" server)

**Reference: Coal Clerk data in Excel file "CoalStats2005.xls" in 1-19-06 e-mail from M.A. Pendley to J.D. Lokey.

Note: fuel oil fired in units 1-2 was apportioned to each unit based on each boiler's proportion of the sub-plant's turbine starts.

TVA Environmental Technologies

7/12/2006

Page 1 of 1
CEMS

CY 2005 CONTINUOUS EMISSION MONITORING SYSTEM (CEMS) DATA*

Paradise Fossil Plant (PAF)

UNIT/

STACK SO2 NOx Heat Input CY05 Coal (Op Stats) Ratio,

Tons/yr lb/10^6 Btu Tons/yr lb/10^6 Btu 10^6 Btu/yr 10^6 Btu/yr CEM/Coal

PAF 1 13,563 0.628 11,466 0.531 43,191,735 42,875,391 1.007

PAF 2 17,320 0.651 14,125 0.531 53,241,517 49,030,801 1.086

PAF 3 53,519 2.31 10,289 0.444 46,316,269 47,329,486 0.979

PAF TOTAL 84,402 1.18 35,879 0.503 142,749,521 139,235,679 1.025

*Reference: Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey.

Data captured (as values) from reference:

SO2 NOx Heat Input

10^3 tons/yr lb/10^6 Btu 10^3 tons/yr lb/10^6 Btu 10^12 Btu/yr

PAF1 13.563 0.628 11.466 0.531 43.191735

PAF2 17.320 0.651 14.125 0.531 53.241517

PAF3 53.519 2.311 10.289 0.444 46.316269

Data captured (as values) from reference:

NOx Heat Input

tons/yr 10^12 Btu/yr OS HI, % of CY05

PAF1 794 18.384697 42.57

PAF2 972 22.270212 41.83

PAF3 1127 26.095902 56.34

TVA Environmental Technologies

07/12/06

ANNUAL

OZONE SEASON (OS)

Page 1 of 1
coal_qual

CY05 PARADISE FOSSIL PLANT (PAF) COAL BURN QUANTITIES & ANALYSES*

PAF UNITS 1-2 COAL ANALYSIS

SOURCE STATE TONS BURNED W. KY PRB

W. KY (Illinois Basin) coals KY 3,946,354 T.Moist% = 12.2 T.Moist% = 27.5

PRB Wyoming 47,724 Ash% = 8.6 Ash% = 5.3

3,994,078 Sul.% = 2.69 Sul.% = 0.35

Carb% = Carb% =

Hydr% = Hydr% =

Nitr% = Nitr% =

Oxy% = Oxy% =

BTU/lb = 11,500 BTU/lb = 8,775

Cl ppm = 602 Cl ppm = 50

Hg ppm = 0.1076 Hg ppm = 0.105

PAF UNIT 3

SOURCE STATE TONS BURNED COAL ANALYSIS

W. KY (Illinois Basin) coals KY 745,146 W. KY PRB

PRB Wyoming 1,824,322 T.Moist% = 12.2 T.Moist% = 27.5

2,569,468 Ash% = 8.6 Ash% = 5.3

Sul.% = 2.69 Sul.% = 0.35

Carb% = Carb% =

Hydr% = Hydr% =

Nitr% = Nitr% =

Oxy% = Oxy% =

BTU/lb = 11,500 BTU/lb = 8,775

Cl ppm = 602 Cl ppm = 50

Hg ppm = 0.1076 Hg ppm = 0.105

*Reference: Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. (CY05 coal burn, moisture, ash, sulfur, & heat

contents). Note that mercury (Hg) & chloride (Cl) concentrations reflect TVA's CY99 Information Collection Request (ICR) analyses (final compilation

in 3-16-00 e-mail from J.D. Eady to R.W. Burbage), expressed in terms of as-received values (per 2-25-00 conversation between J.D. Eady & J.D. Lokey).

PAF UNITS 1-2

CY05 Usage

% Wt input

Source tons/yr As-fired Dry basis

Western Bituminous (WB) 0 0% 0%

Eastern (App.) Bituminous (AB) 0 0% 0%

PRB Subbituminous (PRB) 47,724 1.2% 1.0%

Illinois Basin Bituminous (ILB) 3,946,354 98.8% 99.0%

Total Burn = 3,994,078 100.0% 100.0%

Analysis, % CY05 Usage

Parameter (Wtd Avg) Source % Ht input

Moisture 12.38 WB 0%

Ash 8.56 AB 0%

Sulfur 2.66 PRB 0.9%

ILB 99.1%

Total 100.0%

Heat value 11,467 Btu/lb

PAF UNIT 3

CY05 Usage

% Wt input

Source tons/yr As-fired Dry basis

Western Bituminous (WB) 0 0% 0%

Eastern (App.) Bituminous (AB) 0 0% 0%

PRB Subbituminous (PRB) 1,824,322 71.0% 66.9%

Illinois Basin Bituminous (ILB) 745,146 29.0% 33.1%

Total Burn = 2,569,468 100% 100%

Analysis, % CY05 Usage

Parameter (Wtd Avg) Source % Ht input

Moisture 23.06 WB 0%

Ash 6.26 AB 0%

Sulfur 1.03 PRB 65.1%

ILB 34.9%

Total 100.0%

TVA Environmental Technologies

Heat value 9,565 Btu/lb 07/12/06

Page 1 of 1
stk_test

Log Of Stack Testing Results*

Paradise Fossil Plant - Unit 1

Run #1 Run #2 Run #3 Run #4 Average

Particulates Load Particulates Load Particulates Load Particulates Load Particulates Comments

Testing Date(s) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu)

12/14/05 0.066 696.2 0.062 695.8 0.068 692.7 0.065 CY05

09/14/05 0.101 696.7 0.086 696.1 0.082 697.1 0.090 Avg =

05/25/05 0.096 701.3 0.085 701.1 0.074 696.7 0.085 0.077

02/09/05 0.061 704 0.07 704 0.066 703 0.066

12/08/04 0.074 701 0.062 700 0.071 702 0.069 CY04

09/15/04 0.064 692 0.062 691 0.067 693 0.064 Avg =

06/26/04 0.042 676 0.054 676 0.065 676 0.053 0.066

03/04/04 0.083 708 0.074 708 0.072 709 0.076

01/06/04 0.085 700 0.066 701 0.058 701 0.07

09/10/03 0.081 635 0.089 631 0.079 631 0.083

06/17/03 0.075 684 0.093 684 0.084 651 0.084

04/15/03 0.111 665 0.108 665 0.1 664 0.106

12/1702 0.106 645 0.09 642 0.092 641 0.096

09/06/02 0.07 627.4 0.092 627.9 0.069 629.2 0.077

06/25/02 0.04 660.4 0.034 662.7 0.039 663.1 0.038

03/20/02 0.063 688.2 0.082 687.2 0.095 688.7 0.067 688.7 0.077

11/14/01 0.097 675.5 0.048 675.2 0.054 675.7 0.048 674.8 0.066

09/13/01 0.038 657.2 0.046 657.3 0.047 657.7 0.046

06/13/01 0.111 664.2 0.05 664.5 0.029 663.7 0.075

03/14/01 0.063 684.4 0.062 683 0.046 683.2 0.057

01/03/01 0.059 681 0.045 681 0.052 680 0.053

09/13/00 0.049 590 0.058 590 0.053 588 0.053

05/02/00 0.063 664 0.034 664 0.047 663 0.048

02/23/00 0.055 650 0.049 650 0.056 651 0.053

12/28/99 0.054 620 0.058 621 0.037 622 0.050

08/17/99 0.054 643 0.061 644 0.049 644 0.055

04/22/99 0.062 683 0.058 681 0.077 683 0.066

02/10/99 0.051 682 0.045 681 0.043 682 0.046

09/04/98 0.055 629 0.062 629 0.059 628 0.059

07/08/98 0.064 652 0.047 651 0.052 650 0.054

06/24/98 0.042 654 0.063 656 0.064 656 0.056

01/21/98 0.054 628 0.045 624 0.040 642 0.046

04/15/97 0.061 683 0.055 684 0.062 683 0.059

2/6/1997 0.073 688 0.039 681 0.030 681 0.047

10/1/1996 0.035 663 0.039 663 0.033 660 0.036

7/18/1996 0.044 666 0.050 666 0.041 665 0.045

05/15/96 0.053 673 0.057 674 0.058 674 0.056

02/28/96 0.057 680 0.041 678 0.033 680 0.044

12/15/95 0.042 696 0.036 696 0.045 696 0.041

8/23/1995 0.051 645 0.048 644 0.044 644 0.048

6/13/1995 0.041 660 0.039 660 0.039 660 0.040

11/08/94 0.087 658 0.047 659 0.049 659 0.061

9/1/1994 0.038 627 0.045 627 0.036 638 0.040

05/18/94 0.058 676 0.053 679 0.048 675 0.053

Page 1 of 3
stk_test

Paradise Fossil Plant - Unit 2

Run #1 Run #2 Run #3 Run #4 Average

Particulates Load Particulates Load Particulates Load Particulates Load Particulates Comments

Testing Date(s) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu)

12/15/05 0.072 664.5 0.064 663.1 0.063 662.5 0.066 CY05

09/15/05 0.077 658.7 0.077 660.1 0.08 659.1 0.078 Avg =

05/26/05 0.09 662.9 0.09 659.9 0.088 661.7 0.089 0.076

02/08/05 0.067 685.8 0.067 686.5 0.074 686.2 0.069

12/09/04 0.066 697 0.064 697 0.065 691 0.065 CY04

09/14/04 0.064 617 0.076 618 0.075 618 0.072 Avg =

06/24/04 0.061 637 0.058 637 0.061 635.9 0.06 0.069

03/05/04 0.077 641 0.075 641 0.083 642 0.078

12/18/03 0.073 674 0.087 675 0.076 675 0.079

09/09/03 0.083 649 0.091 647 0.064 649 0.079

05/28/03 0.083 639 0.082 639 0.086 639 0.083

04/14/03 0.108 680 0.12 678 0.101 671 0.110

12/18/02 0.097 637 0.105 637 0.102 637 0.101

09/10/02 0.051 646.4 0.048 646.1 0.046 644.2 0.048

06/26/02 0.045 642.4 0.043 640.2 0.038 642.6 0.042

03/21/02 0.067 666 0.075 666.3 0.062 667.5 0.068

11/15/01 0.043 671 0.054 671.1 0.053 671 0.050

09/11/01 0.048 603.4 0.065 601.6 0.056 605.2 0.056

06/14/01 0.042 616.3 0.043 617.9 0.04 656.1 0.042

03/20/01 0.04 682.5 0.051 683.4 0.048 685.6 0.046

11/21/00 0.082 688.7 0.096 688.8 0.07 689.1 0.083

09/12/00 0.056 661 0.069 663 0.059 666 0.061

05/03/00 0.051 676 0.041 679 0.034 674 0.042

03/07/00 0.059 692 0.023 692 0.08 676 0.054

12/21/99 0.050 676 0.047 672 0.035 685 0.044

08/18/99 0.037 574 0.045 571 0.046 572 0.043

04/29/99 0.059 619 0.062 620 0.05 632 0.057

02/09/99 0.058 620 0.048 625 0.046 621 0.051

09/05/98 0.056 630 0.056 629 0.072 629 0.061

06/23/98 0.034 652 0.042 652 0.052 652 0.043

01/22/98 0.036 627 0.043 629 0.042 629 0.040

04/16/97 0.049 664 0.046 665 0.048 662 0.048

03/05/97 0.000 662 0.04 662 0.054 663 0.031

10/02/96 0.037 673 0.033 673 0.033 671 0.034

07/26/96 0.034 652 0.047 656 0.045 656 0.042

05/16/96 0.057 674 0.058 676 0.054 675 0.056

03/11/96 0.037 662 0.045 688 0.048 676 0.043

09/08/95 0.046 620 0.049 623 0.048 625 0.048

06/14/95 0.039 645 0.041 645 0.047 642 0.042

02/24/95 0.038 658 0.029 653 0.024 652 0.030

09/01/94 0.051 653 0.105 653 0.037 658 0.064

11/09/94 0.054 659 0.037 669 0.034 673 0.042

05/18/94 0.059 667 0.049 669 0.039 663 0.049

03/03/94 0.078 664 0.065 663 0.066 666 0.070

Page 2 of 3
stk_test

Paradise Fossil Plant - Unit 3

Run #1 Run #2 Run #3 Run #4 Average

Particulates Load Particulates Load Particulates Load Particulates Load Particulates Comments

Testing Date(s) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu) (MW) (Lbs/MMBtu)

12/20/05 0.05 1057.9 0.038 1048.3 0.037 1048 0.042

09/07/04 0.028 1030 0.027 1021 0.028 1019 0.028

12/17/03 0.041 1022 0.035 1016 0.033 1022 0.036

09/13/02 0.033 1005.9 0.033 985.2 0.029 988.8 0.032

09/12/01 0.037 1019 0.035 1015.8 0.041 993.7 0.038

09/14/00 0.033 1001 0.038 1004 0.058 1003 0.043

9/15/1999 0.01 962 0.008 964 0.01 965 0.009

09/09/98 0.017 1048 0.023 1047 0.055 1040 0.032

05/21/96 0.010 1060 0.009 1060 0.01 1059 0.010

08/25/95 0.047 1051 0.033 1050 0.031 1040 0.037

08/30/94 0.008 1063 0.002 1051 0.003 1043 0.004

*Reference: Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

TVA Environmental Technologies

07/12/06

Page 3 of 3
alt_fuel

CY05 PAF ALTERNATE-FUEL DATA

Units Reference:

Wood waste burned, 10^3 tons/yr = 0 No CY05 WW burn in PAF boilers (Excel file "A

Pet coke burned, 10^3 tons/yr = 0 Not burned at TVA in CY05.

Tire-derived fuel, 10^3 tons/yr = 0 No CY05 TDF burn in PAF boilers (Excel file "A

Limestone flux in boiler, 10^3 tons/yr = 0 PAF1-3 Not added to PAF boilers in CY05 (Excel file "A

Used oil burned, gal/yr = 32,685 PAF1-3 Excel file "PAFAtt1 Oper StatsReport CY 2005.

Lightoff oil burned, gal/yr = 358,923 PAF 1-3 Excel file "CY05 Operating Statistics from Data

Used boiler cleaning chemicals burned, gal/yr = 0 PAF1-3 Word file "2005 Chemicals used for Fossil Boile

Number of rinses per boiler cleaning = 4 per 4-5-04 email from H.G. Evans to S.S. Koss 

Heat Value, Reported Total Analyte Concentration (or MDL), mg/kg

Sample ID Sample Description Btu/lb Arsenic (As)Cadmium (Cd)

Minimum Detectn Limit (MDL) 2.5 0.12

Ball mill gear lube oil 19815 < MDL < MDL

Ball mill mixed shop oil 19339 < MDL < MDL

Basment Elec. shop EPA 2000 19995 < MDL 1.3

Boiler Feed Pump Turbines 19724 < MDL < MDL

Fab shop EPA 2000 19972 < MDL < MDL

Fab Shop used oil 19448 < MDL 0.48

Forced Draft Fans 19739 < MDL 0.42

Hampton shop EPA 2000 17634 < MDL 1.3

Hampton shop used oil 14668 < MDL < MDL

Hed mixed shop oil 19302 < MDL 0.14

Lighting off oil 19260 < MDL < MDL

Main turbine oil tank 19733 < MDL < MDL

MIXED SHOP OIL FROM OIL ANALYSIS 19592 < MDL < MDL

OIL SPILL @ Q-1 HUT 4-15-03 11484 < MDL < MDL

Pdm lab 19327 < MDL < MDL

Prep plant mixed shop oil 19551 < MDL < MDL

Scrubber mixed shop oil 19682 < MDL < MDL

Seal Oil System 7082 < MDL < MDL

Yard mixed oil 19797 < MDL < MDL

Number of samples

Number of detects

Mean

Maximum

Page 1
alt_fuel

*Reference: Excel file "USEDOIL_FPG Reported in CY 03.xls" in 3-4-04 e-mail from M.F. Broder to J.D. Lokey et al.; CY05 a

Table 2. Nominal Used-Oil Parameters*

Specific gravity 0.9 g/mL

Density 7.5 lb/gal

Ash content 0.1 weight %

Sulfur content 0.4 weight %

*Used-oil specific gravity: 3-26-98 phone communication between D.M. Varnell & J.D. Lokey; ash content is nominal value (n

Table 3. AP-42 Uncontrolled Emission Factors for Used Oil Burned in Boilers*

Criteria/Non-HAP Pollutants lb/10^3 gal

Filterable particulate matter (PM_fil) 64 *A (multiply factor times ash content, weight %)

PM < 10-micrometers (PM10_fil) 51 *A

Sulfur dioxide (SO2) 147 *S (multiply factor times sulfur content, weight %)

Nitrogen oxides (NOx) 19

Carbon monoxide (CO) 5

Volatile organic compds (VOC) 1

Lead (Pb) 55 *L (multiply factor times lead content, weight %)

Carbon dioxide (CO2) 22,000

Trace-Element/HAP lb/10^3 gal

Antimony (Sb) BDL BDL = Below detection limit

Arsenic (As) 1.1E-01

Beryllium (Be) BDL

Cadmium (Cd) 9.3E-03

Chromium (Cr) 2.0E-02

Cobalt (Co) 2.1E-04

Manganese (Mn) 6.8E-02

Nickel (Ni) 1.1E-02

Selenium (Se) BDL

Phosphorus (P) ND ND = No data

Hydrogen Chloride (HCl) 66 *Cl (multiply factor times chlorine content, weight %)

*Reference: US EPA, AP-42, 5th Edition, Supplement B, Section 1.11, Waste Oil Combustion, 10-96

Arsenic (As) was not detected above the MDL in a recent 3-year set of TVA's used-oil analyses (CY98 & CY00-01), & TVA ha

Therefore, the TRI team decided to consider As concentrations to be zero in accord with EPA guidance. Cd, Cr, Pb, PCB, & 

recent 3-year set of analyses, so non-detects were adjusted to be equal to 0.5 x MDL for TRI purposes. Total halogen analys

No PCB emission factor is available for used-oil combustion, and none of the CY03 PAF used-oil samples were above the de

Potential (uncontrolled) CY05 PAF used-oil emissions were estimated using AP-42 emission factors, CY03 PAF used-oil anal

Table 4. PAF CY05 Used-Oil Air Emission Estimates

Plant Total

Uncontrolled Emissn, Controlled Emissions, ton/yr

Trace Element ton/yr PAF1 PAF2

Cd 2.89E-05 7.57E-07 0.00E+00

Page 2
alt_fuel

Cr 8.79E-05 5.54E-07 0.00E+00

Co 3.43E-06 2.05E-08 0.00E+00

Pb 2.97E-04 3.03E-06 0.00E+00

Mn 1.11E-03 5.95E-06 0.00E+00

Ni 1.80E-04 9.65E-07 0.00E+00

HCl 1.93E-02 2.90E-04 0.00E+00

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) 1.05E-01 2.00E-03 0.00E+00

PM < 10-micrometers (PM10_fil) 8.33E-02 8.32E-03 0.00E+00

Sulfur dioxide (SO2) 9.61E-01 6.83E-02 0.00E+00

Nitrogen oxides (NOx) 3.11E-01 5.76E-02 0.00E+00

Carbon monoxide (CO) 8.17E-02 4.08E-02 0.00E+00

Volatile organic compds (VOC) 1.63E-02 8.17E-03 0.00E+00

Note (1): Trace element emissions from used oil combustion are presumed to be captured by the air pollution control system 

Note (2): Per TRI team decision, CY05 used-oil emissions were estimated using CY03 PAF used-oil analyses & CY05 used-o

Table 5. PISCES Database Elemental Analyses for Limestone*

Trace-Element Concentrations, mg/kg (dry basis)

Chemical CAS Average Std. Dev. Maximum

Substance Number Median (x) (s) (max)

Antimony (Sb) 7440360 0.72 42 177 1000

Arsenic (As) 7440382 1.4 2.9 3 11

Barium (Ba) 7440393 15 32 34 112

Beryllium (Be) 7440417 0.15 0.56 1.1 6

Cadmium (Cd) 7440439 0.29 0.42 0.35 1.3

Chlorine (Cl) 16887006 155 276 422 2030

Chromium (Cr) 7440473 5.3 6.8 5.2 18

Cobalt (Co) 7440484 0.5 1.4 1.7 6.2

Copper (Cu) 7440508 2.3 4.9 5.7 27

Fluorine (F) 39339850 110 155 139 526

Lead (Pb) 7439921 1.6 2.9 4.9 26

Manganese (Mn) 7439965 80 113 77 290

Mercury (Hg) 7439976 0.0085 0.039 0.13 1

Molybdenum (Mo) 7439987 2.5 13 22 61

Nickel (Ni) 7440020 3.4 6.1 8.3 43

Selenium (Se) 7782492 1.3 1.5 1.3 4.7

Silver (Ag) 7440224 0.91 1.5 1.5 5

Sulfur (S) 7704349 400 937 1080 3600

Thallium (Tl) 7440280 2.6 2.2 0.98 3.1

Vanadium (V) 7440622 5 8 6.9 28

Zinc (Zn) 7440666 17 27 37 200

Source: EPRI PISCES Database (February, 2003)

Notes: The concentrations presented in the tables were calculated using one half of the detection limits for all nondetected va

Nondetected values (represented by one half the detection limit) greater than two times the highest detected concentration

were removed from the data set before statistics were calculated.

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All data that are designated as "poor" or "unacceptable" quality in the PISCES Database were excluded from all calculations.

All "unknown" quality data were included in the calculations. 

Chlorine and fluorine concentrations measured in the coal and fuel oil analyses are normally reported as chloride and fluoride

However, because the forms of these elements present in the fuels are not known, the elemental designations of fluorine and

chlorine have been used in reporting the concentrations in the tables.

*Reference: EPRI LARK-TRIPP Emission Estimation Model, RY2005 Version 1, 3-29-06.

Table 6. PAF CY05 Limestone Air Emission Estimates

Plant Total

Uncontrolled Emissn, Controlled Emissions, ton/yr

Trace Element ton/yr PAF1 PAF2 PAF3

Sb 0.00E+00 0.00E+00 0.00E+00 0.00E+00

As 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Ba 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Be 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Cd 0.00E+00 0.00E+00 0.00E+00 0.00E+00

HCl 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Cr 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Co 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Cu 0.00E+00 0.00E+00 0.00E+00 0.00E+00

HF 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Pb 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Mn 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Hg 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Mo 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Ni 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Se 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Ag 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Tl 0.00E+00 0.00E+00 0.00E+00 0.00E+00

V 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Zn 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Note: Trace element emissions from limestone flux addition to the boilers are presumed to be captured by the air pollution

control system with the same efficiency as those elements released from coal combustion.

No limestone flux addition to PAF boilers in CY05 (Excel file "Alternative Fuels TRI Data CY2005.xls," in 2-3-06 e-mail from S

Table 7. Tire-Derived Fuel (TDF) Trace-Element Emission Parameters*

Uncontrolled TDF *Reference: US EPA, "Air Emissions from Scrap Tire Combustion", 

Emission Factor, EPA-600/R-97-115, October 1997.

Trace Element lb/10^6 Btu

Sb 1.24E-05

As 2.17E-04 CY03 Proximate Analyses for Allen Fossil Plant (ALF) TDF Receipts

Be 2.93E-07

Cd 6.21E-06 Avg. Heat Value = 16,363

Cr 2.27E-05 Avg. SO2 Equivalent = 1.86

Pb 3.86E-04 Avg. Ash Content = 6.26

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Mn 3.40E-05 Avg. Sulfur Content = 1.56

Ni 2.05E-05 Avg. H2O Content = 1.89

Se 2.65E-05

Zn 2.08E-01 Reference: Excel file "Alternative Fuels TRI Data CY2003.xls" in 2-6-04 e

Table 8. PAF CY05 TDF Air Emission Estimates

(assuming TDF is added to the boiler units in proportion to coal burned) 

Plant Total

Uncontrolled Emissn, Controlled Emissions, ton/yr

Trace Element ton/yr PAF1 PAF2

Sb 0.00E+00 0.00E+00 0.00E+00

As 0.00E+00 0.00E+00 0.00E+00

Be 0.00E+00 0.00E+00 0.00E+00

Cd 0.00E+00 0.00E+00 0.00E+00

Cr 0.00E+00 0.00E+00 0.00E+00

Pb 0.00E+00 0.00E+00 0.00E+00

Mn 0.00E+00 0.00E+00 0.00E+00

Ni 0.00E+00 0.00E+00 0.00E+00

Se 0.00E+00 0.00E+00 0.00E+00

Zn 0.00E+00 0.00E+00 0.00E+00

Criteria/Non-HAP Pollutants

Particulate matter (PM) 0.00E+00 0.00E+00 0.00E+00

Sulfur dioxide (SO2) 0.00E+00 0.00E+00 0.00E+00

Note 1: Trace element emissions from TDF combustion (if such were to occur) are presumed to be captured by the air pollutio

the same efficiency as those elements released from coal combustion.

Note 2: No TDF-specific emission factors were available for nitrogen oxides (NOx), carbon monoxide (CO), or volatile organic 

Table 9. PAF Boiler Distillate Lightoff-Oil Emission Factors*

AP-42 Uncontrolled Emission Factors

for Distillate Fuel Oil Combustion,

Trace Element lb/10^12 Btu

Sb 22 *Reference: US EPA's Compilation of Air Pollutant Emission Factors

As 4 5th Edition, Supplement E, 9-98 (Section 1.3, "Fuel Oil Comb

Ba 20 (for Sb, Ba, Co, Mo, and V) AP-42, Vol. I, 5th Edition, Supple

Be 3 (Section 3.1, "Stationary Gas Turbines for Electricity Genera

Cd 3

Cr 3

Co 9.1

Cu 6

Pb 9

Mn 6

Hg 3

Mo 8.4

Ni 3

Se 15

V 4.4

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Zn 4

Organic HAP (CAS Number) lb/10^3 gal

Formaldehyde (50000) 0.061

Polycyclic organic matter (POM) 0.0033

Criteria/Non-HAP Pollutants lb/10^3 gal

Filterable particulate matter (PM_fil) 2

PM < 10-micrometers (PM10_fil) 1

PM < 2.5-micrometers (PM2.5_fil) 0.25

Condensable PM (PM_cond) 1.3

Sulfur dioxide (SO2) 142 * %S

Nitrogen oxides (NOx) 24

Carbon monoxide (CO) 5

Volatile organic compds (VOC) 0.2

Sulfur trioxide (SO3) 5.7 *%S

%S = weight % sulfur in fuel oil

Assume all SO3 is converted to H2SO4.

Table 10. PAF CY05 Lightoff-Oil Usage/Analyses

PAF1-3

PAF1 PAF2 PAF3 Total

Usage, gallons/yr 134,967 44,989 178,967 358,923

Heat Value, Btu/gal 138,500 138,500 138,500 138,500

Sulfur Content, % 0.2 0.2 0.2 0.2

Table 11. PAF CY05 Lightoff-Oil Air Emission Estimates, tons/yr

PAF1-3

Trace Element PAF1 PAF2 PAF3 Total

Sb 2.06E-04 6.85E-05 2.73E-04 5.47E-04

As 3.74E-05 1.25E-05 4.96E-05 9.94E-05

Ba 1.87E-04 6.23E-05 2.48E-04 4.97E-04

Be 2.80E-05 9.35E-06 3.72E-05 7.46E-05

Cd 2.80E-05 9.35E-06 3.72E-05 7.46E-05

Cr 2.80E-05 9.35E-06 3.72E-05 7.46E-05

Co 8.51E-05 2.84E-05 1.13E-04 2.26E-04

Cu 5.61E-05 1.87E-05 7.44E-05 1.49E-04

Pb 8.41E-05 2.80E-05 1.12E-04 2.24E-04

Mn 5.61E-05 1.87E-05 7.44E-05 1.49E-04

Hg 2.80E-05 9.35E-06 3.72E-05 7.46E-05

Mo 7.85E-05 2.62E-05 1.04E-04 2.09E-04

Ni 2.80E-05 9.35E-06 3.72E-05 7.46E-05

Se 1.40E-04 4.67E-05 1.86E-04 3.73E-04

V 4.11E-05 1.37E-05 5.45E-05 1.09E-04

Zn 3.74E-05 1.25E-05 4.96E-05 9.94E-05

Organic HAP (CAS Number)

Formaldehyde (50000) 4.12E-03 1.37E-03 5.46E-03 1.09E-02

Polycyclic organic matter (POM) 2.23E-04 7.42E-05 2.95E-04 5.92E-04

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Criteria/Non-HAP Pollutants

PM_fil 1.35E-01 4.50E-02 1.79E-01 3.59E-01

PM10_fil 6.75E-02 2.25E-02 8.95E-02 1.79E-01

PM2.5_fil 1.69E-02 5.62E-03 2.24E-02 4.49E-02

PM_cond 8.77E-02 2.92E-02 1.16E-01 2.33E-01

SO2 1.92E+00 6.39E-01 2.54E+00 5.10E+00

NOx 1.62E+00 5.40E-01 2.15E+00 4.31E+00

CO 3.37E-01 1.12E-01 4.47E-01 8.97E-01

VOC 1.35E-02 4.50E-03 1.79E-02 3.59E-02

H2SO4 9.42E-02 3.14E-02 1.25E-01 2.51E-01

Distillate fuel oil is fired for lightoff during unit startup (and may also be fired at other times to ensure flame stability).

During the oil-fired portion of unit startup, the electrostatic precipitators on PAF Unit 3 are not energized due to safety concern

Consequently, lightoff-oil emission estimates reflect AP-42 uncontrolled emission factors for distillate fuel oil combustion.

Table 12. Woodwaste (WW) Emission Parameters*

AP-42 WW (Wet Wood) Emission Factors, lb/10^6 Btu *Reference: US EPA, AP-42, 5th Edition, Supplement G, Se

Pollutant Uncontrolled Controlled

Criteria/Non-HAP Pollutants ESP Scrubber

Filterable particulate matter (PM_fil) 3.30E-01 5.40E-02 6.60E-02

PM < 10-micrometers (PM10_fil) 2.90E-01 4.00E-02 6.50E-02

PM < 2.5-micrometers (PM2.5_fil) 2.50E-01 3.50E-02 6.50E-02

Condensable PM (PM_cond) 1.70E-02 1.70E-02

Sulfur dioxide (SO2) 2.50E-02

Nitrogen oxides (NOx) 2.20E-01

Carbon monoxide (CO) 6.00E-01

Volatile organic compds (VOC) 1.70E-02

Trace Element

Sb 7.90E-06

As 2.20E-05

Ba 1.70E-04

Be 1.10E-06

Cd 4.10E-06

HCl 1.90E-02

Cr 2.10E-05

Co 6.50E-06

Cu 4.90E-05

Pb 4.80E-05

Mn 1.60E-03

Hg 3.50E-06

Mo 2.10E-06

Ni 3.30E-05

Se 2.80E-06

Ag 1.70E-03

V 9.80E-07

Zn 4.20E-04

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Organic HAP (CAS Number)

1,2-Dichloroethane (107062) 2.90E-05

1,2-Dichloropropane (78875) 3.30E-05

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) 8.60E-12

2,3,7,8-Tetrachlorodibenzo-p-furan (51207-31-9) 9.00E-11

2-Butanone (78933) 5.40E-06

2,4-Dinitrophenol (51285) 1.80E-07

2,4,6-Trichlorophenol (88062) < 2.20E-08

4-Nitrophenol (100027) 1.10E-07

Acetaldehyde (75070) 8.30E-04

Acetophenone (98862) 3.20E-09

Acrolein (107028) 4.00E-03

Benzene (71432) 4.20E-03

bis(2-Ethylhexyl)phthalate (117817) 4.70E-08

Bromomethane (74839) 1.50E-05

Carbon tetrachloride (56235) 4.50E-05

Chlorobenzene (108907) 3.30E-05

Chloroform (67663) 2.80E-05

Chloromethane (74873) 2.30E-05

Ethyl benzene (100414) 3.10E-05

Formaldehyde (50000) 4.40E-03

Methyl chloroform (71556) 3.10E-05

Methylene chloride (75092) 2.90E-04

Naphthalene (91203) 9.70E-05

Pentachlorophenol (87865) 5.10E-08

Phenol (108952) 5.10E-05

Propionaldehyde (123386) 6.10E-05

Styrene (100425) 1.90E-03

Tetrachloroethylene (127184) 3.80E-05

Toluene (108883) 9.20E-04

Trichloroethylene (79016) 3.00E-05

Vinyl chloride (75014) 1.80E-05

o-Xylene (95476) 2.50E-05

Polychlorinated biphenyls [PCB] (1336363): 8.15E-09

Monochlorobiphenyl 2.20E-10

Dichlorobiphenyl 7.40E-10

Trichlorobiphenyl 2.60E-09

Tetrachlorobiphenyl 2.50E-09

Pentachlorobiphenyl 1.20E-09

Hexachlorobiphenyl 5.50E-10

Heptachlorobiphenyl 6.60E-11

Decachlorobiphenyl 2.70E-10

Polychlorinated dibenzo-p-dioxins (PCDD): 1.67E-06

Tetrachlorodibenzo-p-dioxins 4.70E-10

Pentachlorodibenzo-p-dioxins 1.50E-09

Hexachlorodibenzo-p-dioxins 1.60E-06

Heptachlorodibenzo-p-dioxins 2.00E-09

Octachlorodibenzo-p-dioxins 6.60E-08

Polychlorinated dibenzo-p-furans (PCDF): 1.78E-09

Tetrachlorodibenzo-p-furans 7.50E-10

Pentachlorodibenzo-p-furans 4.20E-10

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Hexachlorodibenzo-p-furans 2.80E-10

Heptachlorodibenzo-p-furans 2.40E-10

Octachlorodibenzo-p-furans 8.80E-11

Polycyclic organic matter (POM): 4.53E-05

2-Chloronaphthalene (91-58-7) 2.40E-09

2-Methylnaphthalene (91-57-6) 1.60E-07

Acenaphthene (83-32-9) 9.10E-07

Acenaphthylene (208-96-8) 5.00E-06

Anthracene (120-12-7) 3.00E-06

Benzo(a)anthracene (56-55-3) 6.50E-08

Benzo(a)pyrene (50-32-8) 2.60E-06

Benzo(b)fluoranthene (205-99-2) 1.00E-07

Benzo(k)fluoranthene (207-08-9) 3.60E-08

Benzo(j,k)fluoranthene 1.60E-07

Benzo(e)pyrene (192-97-2) 2.60E-09

Benzo(g,h,i)perylene (191-24-2) 9.30E-08

Carbazole (86-74-8) 1.80E-06

Chrysene (218-01-9) 3.80E-08

Dibenzo(a,h)anthracene (53-70-3) 9.10E-09

Fluoranthene (206-44-0) 1.60E-06

Fluorene (86-73-7) 3.40E-06

Indeno(1,2,3,c,d)pyrene (193-39-5) 8.70E-08

Methyl anthracene 1.56E-05 Methyl anthracene emission factor (fr. AP-42 Su

Perylene (198-55-0) 5.20E-10 Supplemt E factor, in lb/(ton of moist, as-fired w

Phenanthrene (85-01-8) 7.00E-06

Pyrene (129-00-0) 3.70E-06

Polycyclic aromatic compounds (PAC) 4.54E-06

Table 13. PAF CY05 WW Air Emission Estimates

(assuming WW is added to the boiler units in proportion to coal burned) 

Species Controlled Emissions, ton/yr

PAF1 PAF2 PAF3

Criteria/Non-HAP Pollutants

PM_fil 0.00E+00 0.00E+00 0.00E+00

PM10_fil 0.00E+00 0.00E+00 0.00E+00

PM2.5_fil 0.00E+00 0.00E+00 0.00E+00

PM_cond 0.00E+00 0.00E+00 0.00E+00

SO2 0.00E+00 0.00E+00 0.00E+00

NOx 0.00E+00 0.00E+00 0.00E+00

CO 0.00E+00 0.00E+00 0.00E+00

VOC 0.00E+00 0.00E+00 0.00E+00

Trace Element

Sb 0.00E+00 0.00E+00 0.00E+00

As 0.00E+00 0.00E+00 0.00E+00

Ba 0.00E+00 0.00E+00 0.00E+00

Be 0.00E+00 0.00E+00 0.00E+00

Cd 0.00E+00 0.00E+00 0.00E+00

Cr 0.00E+00 0.00E+00 0.00E+00

Co 0.00E+00 0.00E+00 0.00E+00

Cu 0.00E+00 0.00E+00 0.00E+00

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Pb 0.00E+00 0.00E+00 0.00E+00

Mn 0.00E+00 0.00E+00 0.00E+00

Mo 0.00E+00 0.00E+00 0.00E+00

Ni 0.00E+00 0.00E+00 0.00E+00

Se 0.00E+00 0.00E+00 0.00E+00

Ag 0.00E+00 0.00E+00 0.00E+00

V 0.00E+00 0.00E+00 0.00E+00

Zn 0.00E+00 0.00E+00 0.00E+00

HCl 0.00E+00 0.00E+00 0.00E+00

Hg 0.00E+00 0.00E+00 0.00E+00

Organic HAP (CAS Number)

1,2-Dichloroethane (107062) 0.00E+00 0.00E+00 0.00E+00

1,2-Dichloropropane (78875) 0.00E+00 0.00E+00 0.00E+00

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) 0.00E+00 0.00E+00 0.00E+00

2,3,7,8-Tetrachlorodibenzo-p-furan (51207-31-9) 0.00E+00 0.00E+00 0.00E+00

2-Butanone (78933) 0.00E+00 0.00E+00 0.00E+00

2,4-Dinitrophenol (51285) 0.00E+00 0.00E+00 0.00E+00

2,4,6-Trichlorophenol (88062) 0.00E+00 0.00E+00 0.00E+00

4-Nitrophenol (100027) 0.00E+00 0.00E+00 0.00E+00

Acetaldehyde (75070) 0.00E+00 0.00E+00 0.00E+00

Acetophenone (98862) 0.00E+00 0.00E+00 0.00E+00

Acrolein (107028) 0.00E+00 0.00E+00 0.00E+00

Benzene (71432) 0.00E+00 0.00E+00 0.00E+00

bis(2-Ethylhexyl)phthalate (117817) 0.00E+00 0.00E+00 0.00E+00

Bromomethane (74839) 0.00E+00 0.00E+00 0.00E+00

Carbon tetrachloride (56235) 0.00E+00 0.00E+00 0.00E+00

Chlorobenzene (108907) 0.00E+00 0.00E+00 0.00E+00

Chloroform (67663) 0.00E+00 0.00E+00 0.00E+00

Chloromethane (74873) 0.00E+00 0.00E+00 0.00E+00

Ethyl benzene (100414) 0.00E+00 0.00E+00 0.00E+00

Formaldehyde (50000) 0.00E+00 0.00E+00 0.00E+00

Methyl chloroform (71556) 0.00E+00 0.00E+00 0.00E+00

Methylene chloride (75092) 0.00E+00 0.00E+00 0.00E+00

Naphthalene (91203) 0.00E+00 0.00E+00 0.00E+00

Pentachlorophenol (87865) 0.00E+00 0.00E+00 0.00E+00

Phenol (108952) 0.00E+00 0.00E+00 0.00E+00

Propionaldehyde (123386) 0.00E+00 0.00E+00 0.00E+00

Styrene (100425) 0.00E+00 0.00E+00 0.00E+00

Tetrachloroethylene (127184) 0.00E+00 0.00E+00 0.00E+00

Toluene (108883) 0.00E+00 0.00E+00 0.00E+00

Trichloroethylene (79016) 0.00E+00 0.00E+00 0.00E+00

Vinyl chloride (75014) 0.00E+00 0.00E+00 0.00E+00

o-Xylene (95476) 0.00E+00 0.00E+00 0.00E+00

Polychlorinated biphenyls [PCB] (1336363): 0.00E+00 0.00E+00 0.00E+00

Polychlorinated dibenzo-p-dioxins (PCDD): 0.00E+00 0.00E+00 0.00E+00

Polychlorinated dibenzo-p-furans (PCDF): 0.00E+00 0.00E+00 0.00E+00

Polycyclic organic matter (POM): 0.00E+00 0.00E+00 0.00E+00

2-Chloronaphthalene (91-58-7) 0.00E+00 0.00E+00 0.00E+00

2-Methylnaphthalene (91-57-6) 0.00E+00 0.00E+00 0.00E+00

Acenaphthene (83-32-9) 0.00E+00 0.00E+00 0.00E+00

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Acenaphthylene (208-96-8) 0.00E+00 0.00E+00 0.00E+00

Anthracene (120-12-7) 0.00E+00 0.00E+00 0.00E+00

Benzo(a)anthracene (56-55-3) 0.00E+00 0.00E+00 0.00E+00

Benzo(a)pyrene (50-32-8) 0.00E+00 0.00E+00 0.00E+00

Benzo(b)fluoranthene (205-99-2) 0.00E+00 0.00E+00 0.00E+00

Benzo(k)fluoranthene (207-08-9) 0.00E+00 0.00E+00 0.00E+00

Benzo(j,k)fluoranthene 0.00E+00 0.00E+00 0.00E+00

Benzo(e)pyrene (192-97-2) 0.00E+00 0.00E+00 0.00E+00

Benzo(g,h,i)perylene (191-24-2) 0.00E+00 0.00E+00 0.00E+00

Carbazole (86-74-8) 0.00E+00 0.00E+00 0.00E+00

Chrysene (218-01-9) 0.00E+00 0.00E+00 0.00E+00

Dibenzo(a,h)anthracene (53-70-3) 0.00E+00 0.00E+00 0.00E+00

Fluoranthene (206-44-0) 0.00E+00 0.00E+00 0.00E+00

Fluorene (86-73-7) 0.00E+00 0.00E+00 0.00E+00

Indeno(1,2,3,c,d)pyrene (193-39-5) 0.00E+00 0.00E+00 0.00E+00

Methyl anthracene 0.00E+00 0.00E+00 0.00E+00

Perylene (198-55-0) 0.00E+00 0.00E+00 0.00E+00

Phenanthrene (85-01-8) 0.00E+00 0.00E+00 0.00E+00

Pyrene (129-00-0) 0.00E+00 0.00E+00 0.00E+00

Polycyclic aromatic compounds (PAC) 0.00E+00 0.00E+00 0.00E+00

Table 14. CY05 Emission Estimates for PAF Evaporation/Combustion of Used EDTA Boiler Cleaning Chemical Solut

PAF Unit 1 Generic EDTA Analysis & Emission Estimates**

All-Composite Mass Control Stack

Concentration, Inputs, Efficiency, Emissns,

Component mg/L lb % tons

Aluminum (Al) 0.8 0.00E+00 90 0.00E+00

Arsenic (As) nd*** 97.83 0.00E+00

Barium (Ba) 0.61 0.00E+00 99.22 0.00E+00

Boron (B) 3.8 0.00E+00 90 0.00E+00

Cadmium (Cd) 0.11 0.00E+00 94.77 0.00E+00

Calcium (Ca) 56.4 0.00E+00 90 0.00E+00

Chromium (Cr) 2.7 0.00E+00 98.74 0.00E+00

Cobalt (Co) 0.4 0.00E+00 98.81 0.00E+00

Copper (Cu) 41.8 0.00E+00 99.14 0.00E+00

Iron (Fe) 1772 0.00E+00 94 0.00E+00

Lead (Pb) 2.0 0.00E+00 97.96 0.00E+00

Magnesium (Mg) 7.4 0.00E+00 90 0.00E+00

Manganese (Mn) 14.0 0.00E+00 98.93 0.00E+00

Molybdenum (Mo) 0.6 0.00E+00 97.89 0.00E+00

Nickel (Ni) 2.8 0.00E+00 98.93 0.00E+00

Phosphorus as (PO4) 102 0.00E+00 90 0.00E+00

Potassium (K) 0.4 0.00E+00 90 0.00E+00

Selenium (Se) nd*** 88.02 0.00E+00

Silicon (Si) 1.8 0.00E+00 90 0.00E+00

Silver (Ag) 0.28 0.00E+00 95.90 0.00E+00

Sodium (Na) 8.2 0.00E+00 90 0.00E+00

Sulfur as Sulfate 10.2 0.00E+00 90 0.00E+00

Tin (Sn) 0.6 0.00E+00 90 0.00E+00

Page 11
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Titanium (Ti) 0.4 0.00E+00 90 0.00E+00

Vanadium (V) 0.2 0.00E+00 99.05 0.00E+00

Zinc (Zn) 30.8 0.00E+00 98.55 0.00E+00

pH 9.3

Spec Gravity 1.04

%residual EDTA 4.6%

***nd = none detected

EDTA Drain Vol = gallons

No.. of Rinses = 4

Volume Burned = 0 gallons

*No PAF EDTA used-boiler-cleaning chemicals were burned in CY05, per Word file "2005 Chemicals used for Fossil Boiler C

Note: First-flush EDTA drain volumes (boiler-tube-volume capacity) for PAF Units 1-2 (142,000 gallons/boiler) and PAF Unit 

in 6-22-98 e-mail from E.W. Zizvari to J.D. Lokey et al.

**Note: "All-composite" concentrations listed above for RCRA analytes (As, Ba, Cd, Cr, Pb, Se, and Ag) reflect TCLP Extract 

 (EDTA + rinsate) from 11-11-02 Colbert Fossil Plant (COF) Unit 1 boiler cleaning. These analyses were deemed "worst-cas

 Concentrations listed for non-RCRA analytes were derived from Hydrochem grab-sample "drain" analyses for 11-11-02 CO

 and do not include rinsate, these concentrations were adjusted to account for volume (EDTA drain + rinsate) that was burne

EDTA is not a TRI chemical. EDTA is decomposed to molecular nitrogen (N2), carbon dioxide (CO2), and water, according to 

During burns of used EDTA boiler-cleaning chemicals in coal-fired boilers, trace elements contained in the solution are report

uniformly among the ash particles formed during coal combustion. Stack tests at oil- & coal-fired boilers during burn/evapora

cleaning chemicals reported by Sisson and Lee (1972) indicated that metals in the EDTA solution are collected by air-pollutio

the same efficiency as applies during normal operation. Tests in an oil-fired boiler equipped with cyclone-type mechanical co

and 90% of Ni injected in the solution were retained in the boiler system. The portion retained in the boiler was assumed to g

emissions due to CY05 burn/evaporation of used boiler-cleaning chemicals in the PAF boiler units (had such occurred) were e

where available, and were otherwise based on conservative values in the Excel file "Boiler cleanings EDTA Evaporated.xls" i

as revised per conversations 7-7-98 and 7-8-98 (renamed "Blr_clean_EDTA_Evap.xls") & included in 7-8-98 e-mail from J.D. 

These efficiencies are supported as being conservative estimates by the following references:

(1) "Incineration Safely Disposes of Chemical Cleaning Solvents", by A.B. Sisson & G.V. Lee, presented at the 34th Annual M

 

(2) "Evaporation in Boiler Furnace", technical literature provided to E.W. Zizvari by representative of Hydrochem Industrial Se

 

(3) "Evaporation Process for Chemical Waste Disposal", technical literature provided by Halliburton Services, Duncan, OK.

Page 12
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RNATE-FUEL DATA

o CY05 WW burn in PAF boilers (Excel file "Alternative Fuels TRI Data CY2005.xls," in 2-3-06 e-mail from S.A. Godbehere to R.W. Burba

ot burned at TVA in CY05.

o CY05 TDF burn in PAF boilers (Excel file "Alternative Fuels TRI Data CY2005.xls," in 2-3-06 e-mail from S.A. Godbehere to R.W. Burba

ot added to PAF boilers in CY05 (Excel file "Alternative Fuels TRI Data CY2005.xls," in 2-3-06 e-mail from S.A. Godbehere to R.W. Burba

xcel file "PAFAtt1 Oper StatsReport CY 2005.xls" in 2-10-06 e-mail from M.A. Pendley to J.D. Lokey.

xcel file "CY05 Operating Statistics from DataFuser (012306).xls" in CY 05\Release Estimates\Operating Stats folder on FPG Env Affr - TR

Word file "2005 Chemicals used for Fossil Boiler Cleanings 1-13-06.doc" in CY 05\Release Estimates\Boiler Cleaning folder on FPG Env Af

er 4-5-04 email from H.G. Evans to S.S. Koss et al. (number of rinses includes passivation step) 

Table 1. CY03 PAF Used-Oil Analyses*

d Total Analyte Concentration (or MDL), mg/kg Adjusted Total Analyte Concentration, mg/kg

Chromium (Cr) Lead (Pb) As Cd Cr Pb

1.2 1.2

< MDL < MDL 0 0.06 0.6 0.6

< MDL 8.5 0 0.06 0.6 8.5

< MDL 1.7 0 1.3 0.6 1.7

< MDL < MDL 0 0.06 0.6 0.6

< MDL < MDL 0 0.06 0.6 0.6

2 11 0 0.48 2 11

< MDL 3.1 0 0.42 0.6 3.1

< MDL 2.3 0 1.3 0.6 2.3

< MDL < MDL 0 0.06 0.6 0.6

< MDL 6.7 0 0.14 0.6 6.7

< MDL < MDL 0 0.06 0.6 0.6

< MDL < MDL 0 0.06 0.6 0.6

< MDL < MDL 0 0.06 0.6 0.6

< MDL < MDL 0 0.06 0.6 0.6

< MDL < MDL 0 0.06 0.6 0.6

1.4 2.9 0 0.06 1.4 2.9

< MDL < MDL 0 0.06 0.6 0.6

< MDL < MDL 0 0.06 0.6 0.6

< MDL 3.2 0 0.06 0.6 3.2

19 19 19 19

0 5 2 8

0 0.236 0.716 2.42

0 1.3 2 11

Page 13
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 from M.F. Broder to J.D. Lokey et al.; CY05 analyses not captured per TRI team decision.

 & J.D. Lokey; ash content is nominal value (no data available); nominal value for TVA used-oil sulfur content provided to TRI team by S.A

n Factors for Used Oil Burned in Boilers*

h content, weight %)

fur content, weight %)

d content, weight %)

hlorine content, weight %)

Oil Combustion, 10-96

sed-oil analyses (CY98 & CY00-01), & TVA has no reason to expect that used oil should be contaminated with As.

cord with EPA guidance. Cd, Cr, Pb, PCB, & total halogen concentrations have been detected in used oil in that

x MDL for TRI purposes. Total halogen analyses were taken to be entirely chlorine to estimate HCl emissions.

Y03 PAF used-oil samples were above the detection limit for PCB, so no PCB emission estimate was made.

-42 emission factors, CY03 PAF used-oil analyses (for Cd, Cr, Pb, and HCl), & CY05 PAF used-oil burn quantities.

 Emission Estimates

PAF1-3 % of PAF3

PAF3 Total Total Emissns

7.40E-07 1.50E-06 0.0031

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4.84E-07 1.04E-06 0.0003

1.53E-08 3.58E-08 0.00004

2.03E-06 5.06E-06 0.0011

4.80E-06 1.08E-05 0.0015

9.81E-07 1.95E-06 0.0006

8.35E-03 8.64E-03 0.0017

1.13E-03 3.12E-03 0.0001

4.69E-03 1.30E-02 0.0008

4.81E-01 5.49E-01 0.0009

6.10E-02 1.19E-01 0.0006

4.09E-02 8.17E-02 0.0064

8.18E-03 1.63E-02 0.0058

e captured by the air pollution control system with the same efficiency as those elements released from coal combustion.

g CY03 PAF used-oil analyses & CY05 used-oil burn quantities.

emental Analyses for Limestone*

centrations, mg/kg (dry basis) Number of

Data Non- Limestone

Minimum x+3s Points Detects H2O, %

0.0025 573 32 17 1

0.66 11.9 39 13 (taken from SHF Title V Permit Applicat

1.3 134 34 10

0.00015 3.86 37 19

0.01 1.47 42 12

22 1542 27 2

0.57 22.4 36 4

0.15 6.5 29 13

1 22 35 9

3 572 32 7

0.1 17.6 41 6

0.02 344 38 0

0.002 0.429 58 36

0.04 79 27 10

1.5 31 33 8

0.086 5.4 42 22

0.91 6 15 13

75 4177 15 1

0.08 5.14 7 2

1.8 28.7 33 6

0.01 138 30 2

alf of the detection limits for all nondetected values.

wo times the highest detected concentration

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Database were excluded from all calculations.

 are normally reported as chloride and fluoride.

wn, the elemental designations of fluorine and

sion Estimates

PAF1-3 % of PAF3

Total Total Emissns

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

0.00E+00 0.00E+00

resumed to be captured by the air pollution

TRI Data CY2005.xls," in 2-3-06 e-mail from S.A. Godbehere to R.W. Burbage et al.).

ement Emission Parameters*

Emissions from Scrap Tire Combustion", 

-115, October 1997.

for Allen Fossil Plant (ALF) TDF Receipts

Btu/lb (as rec'd) 16,678 Btu/lb (dry)

lb SO2/10^6 Btu

% (as received) 6.38 % (dry)

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% (as received) 1.58 % (dry)

%

native Fuels TRI Data CY2003.xls" in 2-6-04 e-mail from S.A. Godbehere to S.S. Koss.

mission Estimates

 in proportion to coal burned) 

trolled Emissions, ton/yr PAF1-3 % of PAF1

PAF3 Total Total Emissns

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

0.00E+00 0.00E+00 0.00

are presumed to be captured by the air pollution control system with

Ox), carbon monoxide (CO), or volatile organic compounds (VOC).

 Lightoff-Oil Emission Factors*

mpilation of Air Pollutant Emission Factors (AP-42), Vol. I,

pplement E, 9-98 (Section 1.3, "Fuel Oil Combustion"); also, 

, Mo, and V) AP-42, Vol. I, 5th Edition, Supplement B, 10-96 

Stationary Gas Turbines for Electricity Generation").

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% of PAF1

Total Emissns

0.82

0.010

0.03

0.07

0.07

0.009

0.12

0.03

0.018

0.011

0.04

0.04

0.008

0.04

0.007

0.003

6.88

0.78

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0.009

0.007

0.003

0.020

0.014

0.014

0.07

0.013

0.010

other times to ensure flame stability).

Unit 3 are not energized due to safety concerns.

on factors for distillate fuel oil combustion.

mission Parameters*

S EPA, AP-42, 5th Edition, Supplement G, Section 1.6, Wood Residue Combustion in Boilers, 3-02 [Update 2003, revised 9-03]

Basis for AP-42 Supplement E (2-99) emission factors:

WW Heating Value = 4500 Btu/lb

WW H2O Content = 50 weight %

CY99 & CY03 WW Analyses** No. of samples

CY03 WW Heat = 4372 Btu/lb (as-received) 27

CY03 WW Total H2O = 45.66 weight % 27

CY03 WW Ash = 5.66 wt. % (as-received) 27

CY03 WW Sulfur = 0.06 wt. % (as-received) 27

CY99 WW Chlorine = 0.151 wt. % (dry) 7

CY99 WW Mercury = 0.029 ppm (dry) 7

**References: Excel file "CY99 BACA Wood analyses.xls" in 1-10-00 e-mail from T.V. Bramlett

to S.M. Deberry, as modified per 3-29-00 e-mail from T.V. Bramlett to J.D. Lokey (CY99 Hg & Cl

analyses); Excel file "Alternative Fuels TRI Data CY2003.xls" downloaded 2-10-04 from "envshr" drive.

drive. (CY03 analyses for sawdust burned at Colbert Fossil Plant [COF]).

Uncontrolled Emission Factors based on CY99/CY03 analyses:

lb/ton WW as fired lb/10^6 Btu

SO2 2.21 0.252

HCl 1.69 0.194

Hg 3.19E-05 3.65E-06

Note controlled filterable PM/PM10/PM2.5 emission factors for wood-fired boilers with electrostatic-precipitator (ESP) PM con

Page 19
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were used for PAF Unit 3, and corresponding emission factors for boilers with wet-scrubber PM control system were used for 

Page 20
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ethyl anthracene emission factor (fr. AP-42 Supplemt E, 2-99) is not contained in AP-42 Supplemt G.

upplemt E factor, in lb/(ton of moist, as-fired wood waste), was converted to lb/10^6 Btu per 4500 Btu/lb moist WW.

W Air Emission Estimates

er units in proportion to coal burned) 

PAF1-3 % of PAF1

Total Total Emissns

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.000

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

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0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 #DIV/0!

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.0000

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

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0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 #DIV/0!

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 #DIV/0!

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

0.00E+00 0.00

Used EDTA Boiler Cleaning Chemical Solutions*

PAF Unit 2 Generic EDTA Analysis & Emission Estimates**

All-Composite Mass Control Stack

Concentration, Inputs, Efficiency, Emissns,

Component mg/L lb % tons

Aluminum (Al) 0.8 0.00E+00 90 0.00E+00

Arsenic (As) nd*** 97.90 0.00E+00

Barium (Ba) 0.61 0.00E+00 99.22 0.00E+00

Boron (B) 3.8 0.00E+00 90 0.00E+00

Cadmium (Cd) 0.11 0.00E+00 94.86 0.00E+00

Calcium (Ca) 56.4 0.00E+00 90 0.00E+00

Chromium (Cr) 2.7 0.00E+00 98.76 0.00E+00

Cobalt (Co) 0.4 0.00E+00 98.83 0.00E+00

Copper (Cu) 41.8 0.00E+00 99.15 0.00E+00

Iron (Fe) 1772 0.00E+00 94 0.00E+00

Lead (Pb) 2.0 0.00E+00 98.01 0.00E+00

Magnesium (Mg) 7.4 0.00E+00 90 0.00E+00

Manganese (Mn) 14.0 0.00E+00 98.95 0.00E+00

Molybdenum (Mo) 0.6 0.00E+00 97.93 0.00E+00

Nickel (Ni) 2.8 0.00E+00 98.94 0.00E+00

Phosphorus as (PO4) 102 0.00E+00 90 0.00E+00

Potassium (K) 0.4 0.00E+00 90 0.00E+00

Selenium (Se) nd*** 88.05 0.00E+00

Silicon (Si) 1.8 0.00E+00 90 0.00E+00

Silver (Ag) 0.28 0.00E+00 95.90 0.00E+00

Sodium (Na) 8.2 0.00E+00 90 0.00E+00

Sulfur as Sulfate 10.2 0.00E+00 90 0.00E+00

Tin (Sn) 0.6 0.00E+00 90 0.00E+00

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Titanium (Ti) 0.4 0.00E+00 90 0.00E+00

Vanadium (V) 0.2 0.00E+00 99.07 0.00E+00

Zinc (Zn) 30.8 0.00E+00 98.57 0.00E+00

pH 9.3

Spec Gravity 1.04

%residual EDTA 4.6%

***nd = none detected

EDTA Drain Vol = gallons

No.. of Rinses = 4

Volume Burned = 0 gallons

 file "2005 Chemicals used for Fossil Boiler Cleanings 1-13-06.doc" in CY 05\Release Estimates\Boiler Cleaning folder on FPG Env Affr - 

its 1-2 (142,000 gallons/boiler) and PAF Unit 3 (143,000 gal) were taken from Excel file "boilercleaning methods vs. plants.xls"

, Cd, Cr, Pb, Se, and Ag) reflect TCLP Extract analyses for used ethylenediamine-tetraacetic-acid (EDTA) boiler-cleaning chemicals

ning. These analyses were deemed "worst-case" for all plants' boiler cleanings (3-13-03 e-mail from S.S. Koss to R.W. Burbage et al.).

grab-sample "drain" analyses for 11-11-02 COF Unit 1 boiler cleaning. Since the "drain" analyses reflect "first-flush" EDTA drain only

volume (EDTA drain + rinsate) that was burned, assuming that the rinsate contributed negligible quantities of metals. 

 carbon dioxide (CO2), and water, according to literature reports.

e elements contained in the solution are reported to be distributed

at oil- & coal-fired boilers during burn/evaporation of used boiler

the EDTA solution are collected by air-pollution-control (APC) equipment at

ler equipped with cyclone-type mechanical collectors found 88% of Cu, 94% of Fe,

ortion retained in the boiler was assumed to go in ash streams to land disposal. Air

he PAF boiler units (had such occurred) were estimated using coal-fired APC control efficiencies

 file "Boiler cleanings EDTA Evaporated.xls" in 6-22-98 e-mail from E.W. Zizvari to J.D. Lokey,

vap.xls") & included in 7-8-98 e-mail from J.D. Lokey to T.A. Burnett, et al.

ng references:

on & G.V. Lee, presented at the 34th Annual Meeting of American Power Conference, Chicago, IL, April 18-20, 1972.

i by representative of Hydrochem Industrial Services, Inc., Crossville, IL.

ovided by Halliburton Services, Duncan, OK.

Page 24
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-mail from S.A. Godbehere to R.W. Burbage et al.).

-mail from S.A. Godbehere to R.W. Burbage et al.).

-mail from S.A. Godbehere to R.W. Burbage et al.).

perating Stats folder on FPG Env Affr - TRI ("Chapgfs5") server

tes\Boiler Cleaning folder on FPG Env Affr - TRI server.

PCB in Used Oil, ppm Total Halogens in Used Oil, ppm

Reported (or MDL) Adjusted Reported (or MDL) Adjusted

1 200

< MDL 0.5 600 600

< MDL 0.5 < MDL 100

< MDL 0.5 300 300

< MDL 0.5 < MDL 100

< MDL 0.5 200 200

< MDL 0.5 400 400

< MDL 0.5 < MDL 100

< MDL 0.5 200 200

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 200 200

< MDL 0.5 < MDL 100

< MDL 0.5 < MDL 100

< MDL 0.5 300 300

19 19

0 7

0.5 179

0.5 600

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ulfur content provided to TRI team by S.A. Godbehere.

minated with As.

 used oil in that

oil burn quantities.

Page 26
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d from coal combustion.

(taken from SHF Title V Permit Application, 12-3-96)

Page 27
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02 [Update 2003, revised 9-03]

No. of samples

Y99 Hg & Cl

rom "envshr" drive.

th electrostatic-precipitator (ESP) PM control system

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crubber PM control system were used for PAF Units 1-2.

Page 32
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 Btu/lb moist WW.

Page 33
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PAF Unit 3 Generic EDTA Analysis & Emission Estimates**

All-Composite Mass Control Stack

Concentration, Inputs, Efficiency, Emissns,

Component mg/L lb % tons

Aluminum (Al) 0.8 0.00E+00 90 0.00E+00

Arsenic (As) nd*** 98.67 0.00E+00

Barium (Ba) 0.61 0.00E+00 99.42 0.00E+00

Boron (B) 3.8 0.00E+00 90 0.00E+00

Cadmium (Cd) 0.11 0.00E+00 94.89 0.00E+00

Calcium (Ca) 56.4 0.00E+00 90 0.00E+00

Chromium (Cr) 2.7 0.00E+00 98.90 0.00E+00

Cobalt (Co) 0.4 0.00E+00 99.11 0.00E+00

Copper (Cu) 41.8 0.00E+00 99.33 0.00E+00

Iron (Fe) 1772 0.00E+00 94 0.00E+00

Lead (Pb) 2.0 0.00E+00 98.63 0.00E+00

Magnesium (Mg) 7.4 0.00E+00 90 0.00E+00

Manganese (Mn) 14.0 0.00E+00 99.14 0.00E+00

Molybdenum (Mo) 0.6 0.00E+00 98.22 0.00E+00

Nickel (Ni) 2.8 0.00E+00 98.91 0.00E+00

Phosphorus as (PO4) 102 0.00E+00 90 0.00E+00

Potassium (K) 0.4 0.00E+00 90 0.00E+00

Selenium (Se) nd*** 69.34 0.00E+00

Silicon (Si) 1.8 0.00E+00 90 0.00E+00

Silver (Ag) 0.28 0.00E+00 97.64 0.00E+00

Sodium (Na) 8.2 0.00E+00 90 0.00E+00

Sulfur as Sulfate 10.2 0.00E+00 90 0.00E+00

Tin (Sn) 0.6 0.00E+00 90 0.00E+00

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Titanium (Ti) 0.4 0.00E+00 90 0.00E+00

Vanadium (V) 0.2 0.00E+00 99.37 0.00E+00

Zinc (Zn) 30.8 0.00E+00 98.45 0.00E+00

pH 9.3

Spec Gravity 1.04

%residual EDTA 4.6%

***nd = none detected

EDTA Drain Vol = gallons

No.. of Rinses = 4

Volume Burned = 0 gallons

\Boiler Cleaning folder on FPG Env Affr - TRI ("chapgfs5") server.

eaning methods vs. plants.xls"

d (EDTA) boiler-cleaning chemicals

om S.S. Koss to R.W. Burbage et al.).

 reflect "first-flush" EDTA drain only

quantities of metals. 

L, April 18-20, 1972.

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PAF Units 1-3 Plant Total EDTA Burn Emission Estimates*

Amount Stack

in Solution, Emissns,

Component lb tons

Aluminum (Al) 0.00E+00 0.00E+00

Arsenic (As) 0.00E+00 0.00E+00

Barium (Ba) 0.00E+00 0.00E+00

Boron (B) 0.00E+00 0.00E+00

Cadmium (Cd) 0.00E+00 0.00E+00

Calcium (Ca) 0.00E+00 0.00E+00

Chromium (Cr) 0.00E+00 0.00E+00

Cobalt (Co) 0.00E+00 0.00E+00

Copper (Cu) 0.00E+00 0.00E+00

Iron (Fe) 0.00E+00 0.00E+00

Lead (Pb) 0.00E+00 0.00E+00

Magnesium (Mg) 0.00E+00 0.00E+00

Manganese (Mn) 0.00E+00 0.00E+00

Molybdenum (Mo) 0.00E+00 0.00E+00

Nickel (Ni) 0.00E+00 0.00E+00

Phosphorus as (PO4) 0.00E+00 0.00E+00

Potassium (K) 0.00E+00 0.00E+00

Selenium (Se) 0.00E+00 0.00E+00

Silicon (Si) 0.00E+00 0.00E+00

Silver (Ag) 0.00E+00 0.00E+00

Sodium (Na) 0.00E+00 0.00E+00

Sulfur as Sulfate 0.00E+00 0.00E+00

Tin (Sn) 0.00E+00 0.00E+00

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Titanium (Ti) 0.00E+00 0.00E+00

Vanadium (V) 0.00E+00 0.00E+00

Zinc (Zn) 0.00E+00 0.00E+00

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PAF1_ILB

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.071 ILB COAL HEAT INPUT (10^12 BTU/YR) = 42.50

UNIT 1 RATED CAPACITY 10^6 BTU/HR 6,959

CY05 ROUTINE ILLINOIS-BASIN (ILB) SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 0.628 DATE: 07/12/06

COAL-FIRED AIR EMISSION ESTIMATES NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.531

BASED ON: ILB COAL H2O (AS-FIRED) % WT (AVG) 12.20 AIR POLLUTION CONTROL SYSTEM(S): VENTURI-FGDW

ILB COAL ASH (AS-FIRED) % WT (AVG) 8.60

CY05 FUEL & CEMS DATA (1) ILB COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 11,500 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

ILB TRACE-ELEMENT CONCENTRATNS (2) ILB COAL SULFUR (AS-FIRED) % WT (AVG) 2.69 PM SO2 NOx

MEDIAN EFH HAP EMISSN FACTRS (3) ILB COAL FIRED (AS-FIRED) TONS 1,847,875 0.11 1.2 NA

AVG OF CY01-CY05 PM STACK TEST DATA (4) ASH SPLIT TO BOTTOM % 75

VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

Hg Contrl Efficiency (%) w/in-service SCR = 86

MEDIAN EFH HOURLY Hg Contrl Efficiency (%) w/o in-service SCR = 18.69

MEDIAN ILB UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS SCR operation factor (total) = 0.485

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.87E+06 7.12E+04 96.19 1514 496 3353 765

PM < 10-micrometer aero. diam. (PM10_fil) NA 2.43E+05 4.84E+04 80.07 1029 337 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 1.03E+05 2.56E+04 75.06 545 178 NA NA

Condensable PM (PM_cond) NA 2.00E+04 425 139 NA NA

Sulfur dioxide (SO2) NA 4.44E+06 6.28E+05 85.87 13545 4371 36577 8351

Nitrogen oxides (NOx) NA 1.43E+06 5.31E+05 63.00 11405 3695 NA NA

Carbon monoxide (CO) NA 2.17E+04 2.17E+04 0.00 462 151 Comparison w/ 4-28-06 LT Outputs:

Volatile organic compounds (VOC) NA 4.78E+03 4.78E+03 0.00 102 33.3 Air rel, lb/yr % Difference

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 1.33E+05 4.65E+04 65.18 988 323 3,068,600 -55.3

Ammonia (NH3) (6) NA 4.34E+02 4.34E-03 99.999 9.23E-05 3.02E-05

PM Trace-Element HAP

Antimony (Sb) 2.00E+00 1.53E+02 1.16E+00 99.24 2.48E-02 8.11E-03

Arsenic (As) 1.10E+01 8.40E+02 1.82E+01 97.84 3.86E-01 1.26E-01

Beryllium (Be) 2.00E+00 1.53E+02 1.81E+00 98.81 3.85E-02 1.26E-02

Cadmium (Cd) 5.00E-01 3.82E+01 1.99E+00 94.79 4.23E-02 1.38E-02

Chromium (Cr) 1.60E+01 1.22E+03 1.54E+01 98.74 3.26E-01 1.07E-01

Cobalt (Co) 3.70E+00 2.82E+02 3.37E+00 98.81 7.15E-02 2.34E-02

Lead (Pb) 1.40E+01 1.07E+03 2.18E+01 97.96 4.63E-01 1.51E-01

Manganese (Mn) 2.90E+01 2.21E+03 2.37E+01 98.93 5.03E-01 1.65E-01

Nickel (Ni) 1.90E+01 1.45E+03 1.55E+01 98.93 3.30E-01 1.08E-01

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.86E+02 5.38E+04 1.62E+03 97.00 3.43E+01 1.12E+01 68,609 0.05

Hydrogen fluoride (HF) 9.20E+01 7.40E+03 4.44E+02 94.00 9.43E+00 3.09E+00 18,861 0.005

Mercury (Hg) 8.00E-02 6.11E+00 2.97E+00 51.32 6.32E-02 2.07E-02 126 -0.005

Selenium (Se) 1.70E+00 1.30E+02 1.56E+01 88.00 3.31E-01 1.08E-01 662 0.0005

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 0.00E+00 1.89E-02 6.19E-03

1,2-Dibromoethane (106934) NA 2.60E+00 0.00E+00 5.53E-02 1.81E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 0.00E+00 3.19E-02 1.04E-02

1,3-Dichloropropene (542756) NA 7.20E-01 0.00E+00 1.53E-02 5.01E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 0.00E+00 2.34E-02 7.65E-03

2-Butanone (78933) NA 3.10E+00 0.00E+00 6.59E-02 2.16E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 0.00E+00 4.25E-03 1.39E-03

3-Chloropropylene (107051) NA 9.10E+00 0.00E+00 1.93E-01 6.33E-02

4-Methyl-2-pentanone (108101) NA 2.30E+00 0.00E+00 4.89E-02 1.60E-02

4-Methylphenol (106445) NA 1.10E+00 0.00E+00 2.34E-02 7.65E-03

Acetaldehyde (75070) NA 3.20E+00 0.00E+00 6.80E-02 2.23E-02 136 0.003

Acetophenone (98862) NA 1.20E+00 0.00E+00 2.55E-02 8.35E-03 51.0 -0.001

Acrolein (107028) NA 1.90E+00 0.00E+00 4.04E-02 1.32E-02 80.8 0.0002

Benzene (71432) NA 3.90E+00 0.00E+00 8.29E-02 2.71E-02

Benzyl chloride (100447) NA 2.80E-01 0.00E+00 5.95E-03 1.95E-03

Biphenyl (92524) NA 1.60E-01 0.00E+00 3.40E-03 1.11E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 0.00E+00 7.65E-02 2.51E-02

Bromomethane (74839) NA 8.90E-01 0.00E+00 1.89E-02 6.19E-03

Carbon disulfide (75150) NA 1.10E+00 0.00E+00 2.34E-02 7.65E-03

Chlorobenzene (108907) NA 1.60E-01 0.00E+00 3.40E-03 1.11E-03

Chloroethane (75003) NA 5.30E-01 0.00E+00 1.13E-02 3.69E-03

Chloroform (67663) NA 8.00E-01 0.00E+00 1.70E-02 5.57E-03

Chloromethane (74873) NA 1.10E+00 0.00E+00 2.34E-02 7.65E-03

Dibenzofuran (132649) NA 5.80E-01 0.00E+00 1.23E-02 4.04E-03

Dibutylphthalate (84742) NA 1.10E-01 0.00E+00 2.34E-03 7.65E-04

Dimethylphthalate (131113) NA 9.00E-02 0.00E+00 1.91E-03 6.26E-04

Ethyl benzene (100414) NA 8.00E-01 0.00E+00 1.70E-02 5.57E-03

Formaldehyde (50000) NA 2.60E+00 0.00E+00 5.53E-02 1.81E-02

n-Hexane (110543) NA 4.90E-01 0.00E+00 1.04E-02 3.41E-03

Hexachlorobenzene (118741) NA 4.10E-03 0.00E+00 8.71E-05 2.85E-05

Iodomethane (74884) NA 2.00E+00 0.00E+00 4.25E-02 1.39E-02

Isophorone (78591) NA 1.20E+00 0.00E+00 2.55E-02 8.35E-03

Methyl chloroform (71556) NA 6.10E-01 0.00E+00 1.30E-02 4.24E-03

Methyl methacrylate (80626) NA 1.10E+00 0.00E+00 2.34E-02 7.65E-03

Methylene chloride (75092) NA 3.60E+00 0.00E+00 7.65E-02 2.51E-02

Naphthalene (91203) 1.60E+00 6.20E-01 0.00E+00 1.32E-02 4.31E-03

Phenol (108952) 1.20E+01 3.30E+00 0.00E+00 7.01E-02 2.30E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 3.19E-04 1.04E-04

Propionaldehyde (123386) NA 1.90E+00 0.00E+00 4.04E-02 1.32E-02

Styrene (100425) NA 7.00E-01 0.00E+00 1.49E-02 4.87E-03

Tetrachloroethylene (127184) NA 4.20E-01 0.00E+00 8.93E-03 2.92E-03

Toluene (108883) NA 1.70E+00 0.00E+00 3.61E-02 1.18E-02

Vinyl acetate (108054) NA 3.10E-01 0.00E+00 6.59E-03 2.16E-03

Vinyl chloride (75014) NA 7.30E-01 0.00E+00 1.55E-02 5.08E-03

Xylenes (1330207) NA 1.26E+00 0.00E+00 2.68E-02 8.77E-03

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 2.82E-02 9.22E-03

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 8.29E-09 2.71E-09

Organic HAP Total 6.69E+01 0.00E+00 1.42E+00 4.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 1.72E+03 7.29E-02 1.19E-05

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey; CEMS data from

 Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05,TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF1_PRB

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.071 PRB COAL HEAT INPUT (10^12 BTU/YR) = 0.33

UNIT 1 RATED CAPACITY 10^6 BTU/HR 6,959

CY05 ROUTINE POWDER RIVER BASIN (PRB) SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 0.628 DATE: 07/12/06

COAL-FIRED AIR EMISSION ESTIMATES NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.531

BASED ON: PRB COAL H2O (AS-FIRED) % WT (AVG) 27.50 AIR POLLUTION CONTROL SYSTEM(S): VENTURI-FGDW

PRB COAL ASH (AS-FIRED) % WT (AVG) 5.30

CY05 FUEL & CEMS DATA (1) PRB COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 8,775 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

PRB TRACE-ELEMENT CONCENTRATNS (2) PRB COAL SULFUR (AS-FIRED) % WT (AVG) 0.35 PM SO2 NOx

MEDIAN EFH HAP EMISSN FACTRS (3) PRB COAL FIRED (AS-FIRED) TONS 18,585 0.11 1.2 NA

AVG OF CY01-CY05 PM STACK TEST DATA (4) ASH SPLIT TO BOTTOM % 75

VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

MEDIAN EFH HOURLY

MEDIAN PRB UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.51E+06 7.12E+04 95.28 11.6 496 3353 765

PM < 10-micrometer aero. diam. (PM10_fil) NA 1.96E+05 4.84E+04 75.32 7.90 337 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 8.30E+04 2.56E+04 69.12 4.18 178 NA NA

Condensable PM (PM_cond) NA 2.00E+04 3.26 139 NA NA

Sulfur dioxide (SO2) NA 6.98E+05 6.28E+05 10.02 16.3 4371 36577 8351

Nitrogen oxides (NOx) NA 9.69E+05 5.31E+05 45.19 59.1 3695 NA NA

Carbon monoxide (CO) NA 2.85E+04 2.85E+04 0.00 4.65 198 Comparison w/ 4-28-06 LT Outputs:

Volatile organic compounds (VOC) NA 6.27E+03 6.27E+03 0.00 1.02 43.6 Air rel, lb/yr % Difference

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 7.08E+03 2.47E+03 65.18 0.402 17.2 814 -1.2

Ammonia (NH3) (6) NA 5.25E+02 3.94E+00 99.25 6.43E-04 2.74E-02

PM Trace-Element HAP

Antimony (Sb) 1.50E-01 1.24E+01 2.74E-01 97.79 4.47E-05 1.91E-03

Arsenic (As) 1.20E+00 9.91E+01 3.54E+00 96.43 5.77E-04 2.46E-02

Beryllium (Be) 2.50E-01 2.07E+01 2.54E-01 98.77 4.14E-05 1.77E-03

Cadmium (Cd) 1.10E-01 9.09E+00 1.08E+00 88.11 1.76E-04 7.52E-03

Chromium (Cr) 4.30E+00 3.55E+02 8.49E+00 97.61 1.39E-03 5.91E-02

Cobalt (Co) 1.60E+00 1.32E+02 2.31E+00 98.25 3.77E-04 1.61E-02

Lead (Pb) 3.20E+00 2.64E+02 8.45E+00 96.81 1.38E-03 5.88E-02

Manganese (Mn) 1.40E+01 1.16E+03 1.82E+01 98.42 2.97E-03 1.27E-01

Nickel (Ni) 2.90E+00 2.40E+02 7.24E+00 96.98 1.18E-03 5.04E-02

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.90E+01 5.86E+03 1.76E+02 97.00 2.87E-02 1.22E+00 57.3 0.04

Hydrogen fluoride (HF) 5.20E+01 4.52E+03 2.71E+02 94.00 4.43E-02 1.89E+00 88.5 0.005

Mercury (Hg) 6.00E-02 4.96E+00 4.69E+00 5.32 7.65E-04 3.27E-02 1.53 -0.001

Selenium (Se) 7.40E-01 6.11E+01 1.83E+00 97.00 2.99E-04 1.28E-02 0.598 0.0002

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 0.00E+00 1.45E-04 6.19E-03

1,2-Dibromoethane (106934) NA 2.60E+00 0.00E+00 4.24E-04 1.81E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 0.00E+00 2.45E-04 1.04E-02

1,3-Dichloropropene (542756) NA 7.20E-01 0.00E+00 1.17E-04 5.01E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 0.00E+00 1.79E-04 7.65E-03

2-Butanone (78933) NA 3.10E+00 0.00E+00 5.06E-04 2.16E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 0.00E+00 3.26E-05 1.39E-03

3-Chloropropylene (107051) NA 9.10E+00 0.00E+00 1.48E-03 6.33E-02

4-Methyl-2-pentanone (108101) NA 2.30E+00 0.00E+00 3.75E-04 1.60E-02

4-Methylphenol (106445) NA 1.10E+00 0.00E+00 1.79E-04 7.65E-03

Acetaldehyde (75070) NA 3.20E+00 0.00E+00 5.22E-04 2.23E-02 1.04 0.003

Acetophenone (98862) NA 1.20E+00 0.00E+00 1.96E-04 8.35E-03 0.391 0.003

Acrolein (107028) NA 1.90E+00 0.00E+00 3.10E-04 1.32E-02 0.620 0.004

Benzene (71432) NA 3.90E+00 0.00E+00 6.36E-04 2.71E-02

Benzyl chloride (100447) NA 2.80E-01 0.00E+00 4.57E-05 1.95E-03

Biphenyl (92524) NA 1.60E-01 0.00E+00 2.61E-05 1.11E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 0.00E+00 5.87E-04 2.51E-02

Bromomethane (74839) NA 8.90E-01 0.00E+00 1.45E-04 6.19E-03

Carbon disulfide (75150) NA 1.10E+00 0.00E+00 1.79E-04 7.65E-03

Chlorobenzene (108907) NA 1.60E-01 0.00E+00 2.61E-05 1.11E-03

Chloroethane (75003) NA 5.30E-01 0.00E+00 8.64E-05 3.69E-03

Chloroform (67663) NA 8.00E-01 0.00E+00 1.30E-04 5.57E-03

Chloromethane (74873) NA 1.10E+00 0.00E+00 1.79E-04 7.65E-03

Dibenzofuran (132649) NA 5.80E-01 0.00E+00 9.46E-05 4.04E-03

Dibutylphthalate (84742) NA 1.10E-01 0.00E+00 1.79E-05 7.65E-04

Dimethylphthalate (131113) NA 9.00E-02 0.00E+00 1.47E-05 6.26E-04

Ethyl benzene (100414) NA 8.00E-01 0.00E+00 1.30E-04 5.57E-03

Formaldehyde (50000) NA 2.60E+00 0.00E+00 4.24E-04 1.81E-02

n-Hexane (110543) NA 4.90E-01 0.00E+00 7.99E-05 3.41E-03

Hexachlorobenzene (118741) NA 4.10E-03 0.00E+00 6.69E-07 2.85E-05

Iodomethane (74884) NA 2.00E+00 0.00E+00 3.26E-04 1.39E-02

Isophorone (78591) NA 1.20E+00 0.00E+00 1.96E-04 8.35E-03

Methyl chloroform (71556) NA 6.10E-01 0.00E+00 9.95E-05 4.24E-03

Methyl methacrylate (80626) NA 1.10E+00 0.00E+00 1.79E-04 7.65E-03

Methylene chloride (75092) NA 3.60E+00 0.00E+00 5.87E-04 2.51E-02

Naphthalene (91203) 1.60E+00 6.20E-01 0.00E+00 1.01E-04 4.31E-03

Phenol (108952) 1.20E+01 3.30E+00 0.00E+00 5.38E-04 2.30E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 2.45E-06 1.04E-04

Propionaldehyde (123386) NA 1.90E+00 0.00E+00 3.10E-04 1.32E-02

Styrene (100425) NA 7.00E-01 0.00E+00 1.14E-04 4.87E-03

Tetrachloroethylene (127184) NA 4.20E-01 0.00E+00 6.85E-05 2.92E-03

Toluene (108883) NA 1.70E+00 0.00E+00 2.77E-04 1.18E-02

Vinyl acetate (108054) NA 3.10E-01 0.00E+00 5.06E-05 2.16E-03

Vinyl chloride (75014) NA 7.30E-01 0.00E+00 1.19E-04 5.08E-03

Xylenes (1330207) NA 1.26E+00 0.00E+00 2.05E-04 8.77E-03

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 2.16E-04 9.22E-03

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 6.36E-11 2.71E-09

Organic HAP Total 6.69E+01 0.00E+00 1.09E-02 4.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 1.72E+03 5.60E-04 1.19E-05

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey; CEMS data from

 Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF1

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.071 COAL HEAT INPUT (10^12 BTU/YR) = 42.83

UNIT 1 RATED CAPACITY 10^6 BTU/HR 6,959

CY05 ROUTINE ILB/PRB COAL-FIRED SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 0.628 DATE: 07/12/06

AIR EMISSION ESTIMATES BASED ON: NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.531

COAL H2O (AS-FIRED) % WT (AVG) 12.38 AIR POLLUTION CONTROL SYSTEM(S): VENTURI-FGDW

CY05 FUEL & CEMS DATA (1) COAL ASH (AS-FIRED) % WT (AVG) 8.56

ILB/PRB TRACE-ELEMENT CONCENTRATNS (2) COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 11,467 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

MEDIAN EFH HAP EMISSN FACTRS (3) COAL SULFUR (AS-FIRED) % WT (AVG) 2.66 PM SO2 NOx

AVG OF CY01-CY05 PM STACK TEST DATA (4) COAL FIRED TONS 1,866,460 0.11 1.2 NA

ASH SPLIT TO BOTTOM % 75

STACK-EXIT SO3 CONCENTRATN PPM VOL 15.9 VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

Hg Contrl Efficiency (%) w/in-service SCR = 86

MEDIAN EFH HOURLY Hg Contrl Efficiency (%) w/o in-service SCR = 18.63

ILB/PRB WTD-AVG UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS SCR operation factor (total) = 0.485

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.87E+06 7.12E+04 96.18 1525 496 3353 765

PM < 10-micrometer aero. diam. (PM10_fil) NA 2.43E+05 4.84E+04 80.03 1037 337 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 1.03E+05 2.56E+04 75.02 549 178 NA NA

Condensable PM (PM_cond) NA 2.00E+04 428 139 QA/QC: NA NA

Sulfur dioxide (SO2) NA 4.42E+06 6.28E+05 85.78 13561 4371 0 36577 8351

Nitrogen oxides (NOx) NA 1.43E+06 5.31E+05 62.91 11464 3695 0 NA NA

Carbon monoxide (CO) NA 2.18E+04 2.18E+04 0.00 467 152

Volatile organic compounds (VOC) NA 4.79E+03 4.79E+03 0.00 103 33.4

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 1.33E+05 4.61E+04 65.18 988 321

Ammonia (NH3) (6) NA 4.35E+02 3.43E-02 99.99 7.35E-04 2.39E-04

PM Trace-Element HAP

Antimony (Sb) 1.98E+00 1.51E+02 1.16E+00 99.24 2.48E-02 8.06E-03

Arsenic (As) 1.09E+01 8.33E+02 1.80E+01 97.83 3.86E-01 1.26E-01

Beryllium (Be) 1.98E+00 1.51E+02 1.80E+00 98.81 3.86E-02 1.25E-02

Cadmium (Cd) 4.96E-01 3.79E+01 1.98E+00 94.77 4.25E-02 1.38E-02

Chromium (Cr) 1.59E+01 1.21E+03 1.53E+01 98.74 3.28E-01 1.07E-01

Cobalt (Co) 3.68E+00 2.81E+02 3.36E+00 98.81 7.19E-02 2.34E-02

Lead (Pb) 1.39E+01 1.06E+03 2.17E+01 97.96 4.64E-01 1.51E-01

Manganese (Mn) 2.89E+01 2.20E+03 2.36E+01 98.93 5.06E-01 1.64E-01

Nickel (Ni) 1.88E+01 1.44E+03 1.55E+01 98.93 3.31E-01 1.08E-01

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.80E+02 5.34E+04 1.60E+03 97.00 3.44E+01 1.12E+01

Hydrogen fluoride (HF) 9.16E+01 7.37E+03 4.42E+02 94.00 9.48E+00 3.08E+00

Mercury (Hg) 7.98E-02 6.10E+00 2.99E+00 51.02 6.39E-02 2.08E-02

Selenium (Se) 1.69E+00 1.29E+02 1.55E+01 88.02 3.31E-01 1.08E-01

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 0.00E+00 1.91E-02 6.19E-03

1,2-Dibromoethane (106934) NA 2.60E+00 0.00E+00 5.57E-02 1.81E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 0.00E+00 3.21E-02 1.04E-02

1,3-Dichloropropene (542756) NA 7.20E-01 0.00E+00 1.54E-02 5.01E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 0.00E+00 2.36E-02 7.65E-03

2-Butanone (78933) NA 3.10E+00 0.00E+00 6.64E-02 2.16E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 0.00E+00 4.28E-03 1.39E-03

3-Chloropropylene (107051) NA 9.10E+00 0.00E+00 1.95E-01 6.33E-02

4-Methyl-2-pentanone (108101) NA 2.30E+00 0.00E+00 4.93E-02 1.60E-02

4-Methylphenol (106445) NA 1.10E+00 0.00E+00 2.36E-02 7.65E-03

Acetaldehyde (75070) NA 3.20E+00 0.00E+00 6.85E-02 2.23E-02

Acetophenone (98862) NA 1.20E+00 0.00E+00 2.57E-02 8.35E-03

Acrolein (107028) NA 1.90E+00 0.00E+00 4.07E-02 1.32E-02

Benzene (71432) NA 3.90E+00 0.00E+00 8.35E-02 2.71E-02

Benzyl chloride (100447) NA 2.80E-01 0.00E+00 6.00E-03 1.95E-03

Biphenyl (92524) NA 1.60E-01 0.00E+00 3.43E-03 1.11E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 0.00E+00 7.71E-02 2.51E-02

Bromomethane (74839) NA 8.90E-01 0.00E+00 1.91E-02 6.19E-03

Carbon disulfide (75150) NA 1.10E+00 0.00E+00 2.36E-02 7.65E-03

Chlorobenzene (108907) NA 1.60E-01 0.00E+00 3.43E-03 1.11E-03

Chloroethane (75003) NA 5.30E-01 0.00E+00 1.13E-02 3.69E-03

Chloroform (67663) NA 8.00E-01 0.00E+00 1.71E-02 5.57E-03

Chloromethane (74873) NA 1.10E+00 0.00E+00 2.36E-02 7.65E-03

Dibenzofuran (132649) NA 5.80E-01 0.00E+00 1.24E-02 4.04E-03

Dibutylphthalate (84742) NA 1.10E-01 0.00E+00 2.36E-03 7.65E-04

Dimethylphthalate (131113) NA 9.00E-02 0.00E+00 1.93E-03 6.26E-04

Ethyl benzene (100414) NA 8.00E-01 0.00E+00 1.71E-02 5.57E-03

Formaldehyde (50000) NA 2.60E+00 0.00E+00 5.57E-02 1.81E-02

n-Hexane (110543) NA 4.90E-01 0.00E+00 1.05E-02 3.41E-03

Hexachlorobenzene (118741) NA 4.10E-03 0.00E+00 8.78E-05 2.85E-05

Iodomethane (74884) NA 2.00E+00 0.00E+00 4.28E-02 1.39E-02

Isophorone (78591) NA 1.20E+00 0.00E+00 2.57E-02 8.35E-03

Methyl chloroform (71556) NA 6.10E-01 0.00E+00 1.31E-02 4.24E-03

Methyl methacrylate (80626) NA 1.10E+00 0.00E+00 2.36E-02 7.65E-03

Methylene chloride (75092) NA 3.60E+00 0.00E+00 7.71E-02 2.51E-02

Naphthalene (91203) 1.60E+00 6.20E-01 0.00E+00 1.33E-02 4.31E-03

Phenol (108952) 1.20E+01 3.30E+00 0.00E+00 7.07E-02 2.30E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 3.21E-04 1.04E-04

Propionaldehyde (123386) NA 1.90E+00 0.00E+00 4.07E-02 1.32E-02

Styrene (100425) NA 7.00E-01 0.00E+00 1.50E-02 4.87E-03

Tetrachloroethylene (127184) NA 4.20E-01 0.00E+00 8.99E-03 2.92E-03

Toluene (108883) NA 1.70E+00 0.00E+00 3.64E-02 1.18E-02

Vinyl acetate (108054) NA 3.10E-01 0.00E+00 6.64E-03 2.16E-03

Vinyl chloride (75014) NA 7.30E-01 0.00E+00 1.56E-02 5.08E-03

Xylenes (1330207) NA 1.26E+00 0.00E+00 2.70E-02 8.77E-03

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 2.84E-02 9.22E-03

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 8.35E-09 2.71E-09

Organic HAP Total 6.69E+01 0.00E+00 1.43E+00 4.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 1.72E+03 7.35E-02 1.19E-05

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey; CEMS data from

 Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF2_ILB

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.069 ILB COAL HEAT INPUT (10^12 BTU/YR) = 48.26

UNIT 2 RATED CAPACITY 10^6 BTU/HR 6,959

CY05 ROUTINE ILLINOIS-BASIN (ILB) SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 0.651 DATE: 07/12/06

COAL-FIRED AIR EMISSION ESTIMATES NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.531

BASED ON: ILB COAL H2O (AS-FIRED) % WT (AVG) 12.20 AIR POLLUTION CONTROL SYSTEM(S): VENTURI-FGDW

ILB COAL ASH (AS-FIRED) % WT (AVG) 8.60

CY05 FUEL & CEMS DATA (1) ILB COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 11,500 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

ILB TRACE-ELEMENT CONCENTRATNS (2) ILB COAL SULFUR (AS-FIRED) % WT (AVG) 2.69 PM SO2 NOx

MEDIAN EFH HAP EMISSN FACTRS (3) ILB COAL FIRED (AS-FIRED) TONS 2,098,385 0.11 1.2 NA

AVG OF CY01-CY05 PM STACK TEST DATA (4) ASH SPLIT TO BOTTOM % 75

VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

Hg Contrl Efficiency (%) w/in-service SCR = 86

MEDIAN EFH HOURLY Hg Contrl Efficiency (%) w/o in-service SCR = 18.69

MEDIAN ILB UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS SCR operation factor (total) = 0.489

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.87E+06 6.90E+04 96.31 1666 480 3353 765

PM < 10-micrometer aero. diam. (PM10_fil) NA 2.43E+05 4.69E+04 80.69 1133 327 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 1.03E+05 2.49E+04 75.83 600 173 NA NA

Condensable PM (PM_cond) NA 2.00E+04 483 139 NA NA

Sulfur dioxide (SO2) NA 4.44E+06 6.51E+05 85.36 17290 4528 36577 8351

Nitrogen oxides (NOx) NA 1.43E+06 5.31E+05 63.02 14024 3692 NA NA

Carbon monoxide (CO) NA 2.17E+04 2.17E+04 0.00 525 151 Comparison w/ 4-28-06 LT Outputs:

Volatile organic compounds (VOC) NA 4.78E+03 4.78E+03 0.00 115 33.3 Air rel, lb/yr % Difference

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 1.34E+05 4.67E+04 65.10 1126 325 3,489,400 -55.0

Ammonia (NH3) (6) NA 4.55E+02 4.55E-03 99.999 1.10E-04 3.17E-05

PM Trace-Element HAP

Antimony (Sb) 2.00E+00 1.53E+02 1.14E+00 99.25 2.76E-02 7.95E-03

Arsenic (As) 1.10E+01 8.40E+02 1.77E+01 97.90 4.27E-01 1.23E-01

Beryllium (Be) 2.00E+00 1.53E+02 1.75E+00 98.85 4.22E-02 1.22E-02

Cadmium (Cd) 5.00E-01 3.82E+01 1.96E+00 94.87 4.73E-02 1.36E-02

Chromium (Cr) 1.60E+01 1.22E+03 1.51E+01 98.77 3.64E-01 1.05E-01

Cobalt (Co) 3.70E+00 2.82E+02 3.29E+00 98.83 7.95E-02 2.29E-02

Lead (Pb) 1.40E+01 1.07E+03 2.12E+01 98.01 5.12E-01 1.48E-01

Manganese (Mn) 2.90E+01 2.21E+03 2.32E+01 98.95 5.61E-01 1.62E-01

Nickel (Ni) 1.90E+01 1.45E+03 1.53E+01 98.95 3.69E-01 1.06E-01

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.86E+02 5.38E+04 1.62E+03 97.00 3.90E+01 1.12E+01 77,910 0.05

Hydrogen fluoride (HF) 9.20E+01 7.40E+03 4.44E+02 94.00 1.07E+01 3.09E+00 21,418 0.004

Mercury (Hg) 8.00E-02 6.11E+00 2.96E+00 51.60 7.13E-02 2.06E-02 143 -0.004

Selenium (Se) 1.70E+00 1.30E+02 1.56E+01 88.00 3.76E-01 1.08E-01 752 0.0002

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 2.15E-02 6.19E-03

1,2-Dibromoethane (106934) NA 2.60E+00 6.27E-02 1.81E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 3.62E-02 1.04E-02

1,3-Dichloropropene (542756) NA 7.20E-01 1.74E-02 5.01E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 2.65E-02 7.65E-03

2-Butanone (78933) NA 3.10E+00 7.48E-02 2.16E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 4.83E-03 1.39E-03

3-Chloropropylene (107051) NA 9.10E+00 2.20E-01 6.33E-02

4-Methyl-2-pentanone (108101) NA 2.30E+00 5.55E-02 1.60E-02

4-Methylphenol (106445) NA 1.10E+00 2.65E-02 7.65E-03

Acetaldehyde (75070) NA 3.20E+00 7.72E-02 2.23E-02 154 0.0007

Acetophenone (98862) NA 1.20E+00 2.90E-02 8.35E-03 57.9 -0.001

Acrolein (107028) NA 1.90E+00 4.58E-02 1.32E-02 91.7 -0.0006

Benzene (71432) NA 3.90E+00 9.41E-02 2.71E-02

Benzyl chloride (100447) NA 2.80E-01 6.76E-03 1.95E-03

Biphenyl (92524) NA 1.60E-01 3.86E-03 1.11E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 8.69E-02 2.51E-02

Bromomethane (74839) NA 8.90E-01 2.15E-02 6.19E-03

Carbon disulfide (75150) NA 1.10E+00 2.65E-02 7.65E-03

Chlorobenzene (108907) NA 1.60E-01 3.86E-03 1.11E-03

Chloroethane (75003) NA 5.30E-01 1.28E-02 3.69E-03

Chloroform (67663) NA 8.00E-01 1.93E-02 5.57E-03

Chloromethane (74873) NA 1.10E+00 2.65E-02 7.65E-03

Dibenzofuran (132649) NA 5.80E-01 1.40E-02 4.04E-03

Dibutylphthalate (84742) NA 1.10E-01 2.65E-03 7.65E-04

Dimethylphthalate (131113) NA 9.00E-02 2.17E-03 6.26E-04

Ethyl benzene (100414) NA 8.00E-01 1.93E-02 5.57E-03

Formaldehyde (50000) NA 2.60E+00 6.27E-02 1.81E-02

n-Hexane (110543) NA 4.90E-01 1.18E-02 3.41E-03

Hexachlorobenzene (118741) NA 4.10E-03 9.89E-05 2.85E-05

Iodomethane (74884) NA 2.00E+00 4.83E-02 1.39E-02

Isophorone (78591) NA 1.20E+00 2.90E-02 8.35E-03

Methyl chloroform (71556) NA 6.10E-01 1.47E-02 4.24E-03

Methyl methacrylate (80626) NA 1.10E+00 2.65E-02 7.65E-03

Methylene chloride (75092) NA 3.60E+00 8.69E-02 2.51E-02

Naphthalene (91203) 1.60E+00 6.20E-01 1.50E-02 4.31E-03

Phenol (108952) 1.20E+01 3.30E+00 7.96E-02 2.30E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 3.62E-04 1.04E-04

Propionaldehyde (123386) NA 1.90E+00 4.58E-02 1.32E-02

Styrene (100425) NA 7.00E-01 1.69E-02 4.87E-03

Tetrachloroethylene (127184) NA 4.20E-01 1.01E-02 2.92E-03

Toluene (108883) NA 1.70E+00 4.10E-02 1.18E-02

Vinyl acetate (108054) NA 3.10E-01 7.48E-03 2.16E-03

Vinyl chloride (75014) NA 7.30E-01 1.76E-02 5.08E-03

Xylenes (1330207) NA 1.26E+00 3.04E-02 8.77E-03

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 3.20E-02 9.22E-03

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 9.41E-09 2.71E-09

Organic HAP Total 6.69E+01 1.61E+00 4.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 1.66E+03 8.02E-02 1.16E-05

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey; CEMS data from

 Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF2_PRB

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.069 PRB COAL HEAT INPUT (10^12 BTU/YR) = 0.51

UNIT 2 RATED CAPACITY 10^6 BTU/HR 6,959

CY05 ROUTINE POWDER RIVER BASIN (PRB) SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 0.651 DATE: 07/12/06

COAL-FIRED AIR EMISSION ESTIMATES NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.531

BASED ON: PRB COAL H2O (AS-FIRED) % WT (AVG) 27.50 AIR POLLUTION CONTROL SYSTEM(S): VENTURI-FGDW

PRB COAL ASH (AS-FIRED) % WT (AVG) 5.30

CY05 FUEL & CEMS DATA (1) PRB COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 8,775 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

PRB TRACE-ELEMENT CONCENTRATNS (2) PRB COAL SULFUR (AS-FIRED) % WT (AVG) 0.35 PM SO2 NOx

MEDIAN EFH HAP EMISSN FACTRS (3) PRB COAL FIRED (AS-FIRED) TONS 29,233 0.11 1.2 NA

AVG OF CY01-CY05 PM STACK TEST DATA (4) ASH SPLIT TO BOTTOM % 75

VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

MEDIAN EFH HOURLY

MEDIAN PRB UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.51E+06 6.90E+04 95.43 17.7 480 3353 765

PM < 10-micrometer aero. diam. (PM10_fil) NA 1.96E+05 4.69E+04 76.09 12.0 327 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 8.30E+04 2.49E+04 70.08 6.38 173 NA NA

Condensable PM (PM_cond) NA 2.00E+04 5.13 139 NA NA

Sulfur dioxide (SO2) NA 6.98E+05 6.51E+05 6.79 28.9 4528 36577 8351

Nitrogen oxides (NOx) NA 9.69E+05 5.31E+05 45.22 101 3692 NA NA

Carbon monoxide (CO) NA 2.85E+04 2.85E+04 0.00 7.31 198 Comparison w/ 4-28-06 LT Outputs:

Volatile organic compounds (VOC) NA 6.27E+03 6.27E+03 0.00 1.61 43.6 Air rel, lb/yr % Difference

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 7.12E+03 2.48E+03 65.10 0.637 17.3 1284 -0.7

Ammonia (NH3) (6) NA 3.97E+02 2.98E+00 99.25 7.64E-04 2.07E-02

PM Trace-Element HAP

Antimony (Sb) 1.50E-01 1.24E+01 2.69E-01 97.83 6.89E-05 1.87E-03

Arsenic (As) 1.20E+00 9.91E+01 3.45E+00 96.52 8.84E-04 2.40E-02

Beryllium (Be) 2.50E-01 2.07E+01 2.45E-01 98.81 6.29E-05 1.71E-03

Cadmium (Cd) 1.10E-01 9.09E+00 1.06E+00 88.30 2.73E-04 7.40E-03

Chromium (Cr) 4.30E+00 3.55E+02 8.34E+00 97.65 2.14E-03 5.80E-02

Cobalt (Co) 1.60E+00 1.32E+02 2.26E+00 98.29 5.80E-04 1.57E-02

Lead (Pb) 3.20E+00 2.64E+02 8.24E+00 96.89 2.11E-03 5.73E-02

Manganese (Mn) 1.40E+01 1.16E+03 1.79E+01 98.45 4.59E-03 1.24E-01

Nickel (Ni) 2.90E+00 2.40E+02 7.14E+00 97.02 1.83E-03 4.97E-02

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.90E+01 5.86E+03 1.76E+02 97.00 4.51E-02 1.22E+00 90.2 0.04

Hydrogen fluoride (HF) 5.20E+01 4.52E+03 2.71E+02 94.00 6.96E-02 1.89E+00 139.3 0.004

Mercury (Hg) 6.00E-02 4.96E+00 4.69E+00 5.32 1.20E-03 3.27E-02 2.41 -0.001

Selenium (Se) 7.40E-01 6.11E+01 1.83E+00 97.00 4.71E-04 1.28E-02 0.941 -0.0003

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 2.28E-04 6.19E-03

1,2-Dibromoethane (106934) NA 2.60E+00 6.67E-04 1.81E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 3.85E-04 1.04E-02

1,3-Dichloropropene (542756) NA 7.20E-01 1.85E-04 5.01E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 2.82E-04 7.65E-03

2-Butanone (78933) NA 3.10E+00 7.95E-04 2.16E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 5.13E-05 1.39E-03

3-Chloropropylene (107051) NA 9.10E+00 2.33E-03 6.33E-02

4-Methyl-2-pentanone (108101) NA 2.30E+00 5.90E-04 1.60E-02

4-Methylphenol (106445) NA 1.10E+00 2.82E-04 7.65E-03

Acetaldehyde (75070) NA 3.20E+00 8.21E-04 2.23E-02 1.64 0.001

Acetophenone (98862) NA 1.20E+00 3.08E-04 8.35E-03 0.616 0.004

Acrolein (107028) NA 1.90E+00 4.87E-04 1.32E-02 0.975 0.003

Benzene (71432) NA 3.90E+00 1.00E-03 2.71E-02

Benzyl chloride (100447) NA 2.80E-01 7.18E-05 1.95E-03

Biphenyl (92524) NA 1.60E-01 4.10E-05 1.11E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 9.23E-04 2.51E-02

Bromomethane (74839) NA 8.90E-01 2.28E-04 6.19E-03

Carbon disulfide (75150) NA 1.10E+00 2.82E-04 7.65E-03

Chlorobenzene (108907) NA 1.60E-01 4.10E-05 1.11E-03

Chloroethane (75003) NA 5.30E-01 1.36E-04 3.69E-03

Chloroform (67663) NA 8.00E-01 2.05E-04 5.57E-03

Chloromethane (74873) NA 1.10E+00 2.82E-04 7.65E-03

Dibenzofuran (132649) NA 5.80E-01 1.49E-04 4.04E-03

Dibutylphthalate (84742) NA 1.10E-01 2.82E-05 7.65E-04

Dimethylphthalate (131113) NA 9.00E-02 2.31E-05 6.26E-04

Ethyl benzene (100414) NA 8.00E-01 2.05E-04 5.57E-03

Formaldehyde (50000) NA 2.60E+00 6.67E-04 1.81E-02

n-Hexane (110543) NA 4.90E-01 1.26E-04 3.41E-03

Hexachlorobenzene (118741) NA 4.10E-03 1.05E-06 2.85E-05

Iodomethane (74884) NA 2.00E+00 5.13E-04 1.39E-02

Isophorone (78591) NA 1.20E+00 3.08E-04 8.35E-03

Methyl chloroform (71556) NA 6.10E-01 1.56E-04 4.24E-03

Methyl methacrylate (80626) NA 1.10E+00 2.82E-04 7.65E-03

Methylene chloride (75092) NA 3.60E+00 9.23E-04 2.51E-02

Naphthalene (91203) 1.60E+00 6.20E-01 1.59E-04 4.31E-03

Phenol (108952) 1.20E+01 3.30E+00 8.47E-04 2.30E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 3.85E-06 1.04E-04

Propionaldehyde (123386) NA 1.90E+00 4.87E-04 1.32E-02

Styrene (100425) NA 7.00E-01 1.80E-04 4.87E-03

Tetrachloroethylene (127184) NA 4.20E-01 1.08E-04 2.92E-03

Toluene (108883) NA 1.70E+00 4.36E-04 1.18E-02

Vinyl acetate (108054) NA 3.10E-01 7.95E-05 2.16E-03

Vinyl chloride (75014) NA 7.30E-01 1.87E-04 5.08E-03

Xylenes (1330207) NA 1.26E+00 3.23E-04 8.77E-03

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 3.40E-04 9.22E-03

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 1.00E-10 2.71E-09

Organic HAP Total 6.69E+01 1.72E-02 4.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 1.66E+03 8.53E-04 1.16E-05

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey; CEMS data from

 Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF2

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.069 COAL HEAT INPUT (10^12 BTU/YR) = 48.78

UNIT 2 RATED CAPACITY 10^6 BTU/HR 6,959

CY05 ROUTINE ILB/PRB COAL-FIRED SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 0.651 DATE: 07/12/06

AIR EMISSION ESTIMATES BASED ON: NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.531

COAL H2O (AS-FIRED) % WT (AVG) 12.38 AIR POLLUTION CONTROL SYSTEM(S): VENTURI-FGDW

CY05 FUEL & CEMS DATA (1) COAL ASH (AS-FIRED) % WT (AVG) 8.56

ILB/PRB TRACE-ELEMENT CONCENTRATNS (2) COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 11,467 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

MEDIAN EFH HAP EMISSN FACTRS (3) COAL SULFUR (AS-FIRED) % WT (AVG) 2.66 PM SO2 NOx

AVG OF CY01-CY05 PM STACK TEST DATA (4) COAL FIRED TONS 2,127,618 0.11 1.2 NA

ASH SPLIT TO BOTTOM % 75

STACK-EXIT SO3 CONCENTRATN PPM VOL 15.9 VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

Hg Contrl Efficiency (%) w/in-service SCR = 86

MEDIAN EFH HOURLY Hg Contrl Efficiency (%) w/o in-service SCR = 18.63

ILB/PRB WTD-AVG UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS SCR operation factor (total) = 0.489

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.87E+06 6.90E+04 96.30 1684 480 3353 765

PM < 10-micrometer aero. diam. (PM10_fil) NA 2.43E+05 4.69E+04 80.65 1145 327 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 1.03E+05 2.49E+04 75.79 606 173 NA NA

Condensable PM (PM_cond) NA 2.00E+04 488 139 QA/QC: NA NA

Sulfur dioxide (SO2) NA 4.40E+06 6.51E+05 85.23 17319 4528 0 36577 8351

Nitrogen oxides (NOx) NA 1.43E+06 5.31E+05 62.89 14124 3692 0 NA NA

Carbon monoxide (CO) NA 2.18E+04 2.18E+04 0.00 532 152

Volatile organic compounds (VOC) NA 4.80E+03 4.80E+03 0.00 117 33.4

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 1.32E+05 4.62E+04 65.10 1126 321

Ammonia (NH3) (6) NA 4.54E+02 3.58E-02 99.99 8.74E-04 2.49E-04

PM Trace-Element HAP

Antimony (Sb) 1.98E+00 1.51E+02 1.13E+00 99.25 2.76E-02 7.88E-03

Arsenic (As) 1.09E+01 8.33E+02 1.75E+01 97.90 4.27E-01 1.22E-01

Beryllium (Be) 1.98E+00 1.51E+02 1.73E+00 98.85 4.23E-02 1.21E-02

Cadmium (Cd) 4.96E-01 3.79E+01 1.95E+00 94.86 4.75E-02 1.36E-02

Chromium (Cr) 1.59E+01 1.21E+03 1.50E+01 98.76 3.66E-01 1.04E-01

Cobalt (Co) 3.68E+00 2.81E+02 3.28E+00 98.83 8.01E-02 2.28E-02

Lead (Pb) 1.39E+01 1.06E+03 2.11E+01 98.01 5.14E-01 1.47E-01

Manganese (Mn) 2.89E+01 2.20E+03 2.32E+01 98.95 5.65E-01 1.61E-01

Nickel (Ni) 1.88E+01 1.44E+03 1.52E+01 98.94 3.71E-01 1.06E-01

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.80E+02 5.34E+04 1.60E+03 97.00 3.90E+01 1.11E+01

Hydrogen fluoride (HF) 9.16E+01 7.37E+03 4.42E+02 94.00 1.08E+01 3.08E+00

Mercury (Hg) 7.98E-02 6.10E+00 2.97E+00 51.22 7.25E-02 2.07E-02

Selenium (Se) 1.69E+00 1.29E+02 1.54E+01 88.05 3.76E-01 1.07E-01

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 0.00E+00 2.17E-02 6.19E-03

1,2-Dibromoethane (106934) NA 2.60E+00 0.00E+00 6.34E-02 1.81E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 0.00E+00 3.66E-02 1.04E-02

1,3-Dichloropropene (542756) NA 7.20E-01 0.00E+00 1.76E-02 5.01E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 0.00E+00 2.68E-02 7.65E-03

2-Butanone (78933) NA 3.10E+00 0.00E+00 7.56E-02 2.16E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 0.00E+00 4.88E-03 1.39E-03

3-Chloropropylene (107051) NA 9.10E+00 0.00E+00 2.22E-01 6.33E-02

4-Methyl-2-pentanone (108101) NA 2.30E+00 0.00E+00 5.61E-02 1.60E-02

4-Methylphenol (106445) NA 1.10E+00 0.00E+00 2.68E-02 7.65E-03

Acetaldehyde (75070) NA 3.20E+00 0.00E+00 7.80E-02 2.23E-02

Acetophenone (98862) NA 1.20E+00 0.00E+00 2.93E-02 8.35E-03

Acrolein (107028) NA 1.90E+00 0.00E+00 4.63E-02 1.32E-02

Benzene (71432) NA 3.90E+00 0.00E+00 9.51E-02 2.71E-02

Benzyl chloride (100447) NA 2.80E-01 0.00E+00 6.83E-03 1.95E-03

Biphenyl (92524) NA 1.60E-01 0.00E+00 3.90E-03 1.11E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 0.00E+00 8.78E-02 2.51E-02

Bromomethane (74839) NA 8.90E-01 0.00E+00 2.17E-02 6.19E-03

Carbon disulfide (75150) NA 1.10E+00 0.00E+00 2.68E-02 7.65E-03

Chlorobenzene (108907) NA 1.60E-01 0.00E+00 3.90E-03 1.11E-03

Chloroethane (75003) NA 5.30E-01 0.00E+00 1.29E-02 3.69E-03

Chloroform (67663) NA 8.00E-01 0.00E+00 1.95E-02 5.57E-03

Chloromethane (74873) NA 1.10E+00 0.00E+00 2.68E-02 7.65E-03

Dibenzofuran (132649) NA 5.80E-01 0.00E+00 1.41E-02 4.04E-03

Dibutylphthalate (84742) NA 1.10E-01 0.00E+00 2.68E-03 7.65E-04

Dimethylphthalate (131113) NA 9.00E-02 0.00E+00 2.19E-03 6.26E-04

Ethyl benzene (100414) NA 8.00E-01 0.00E+00 1.95E-02 5.57E-03

Formaldehyde (50000) NA 2.60E+00 0.00E+00 6.34E-02 1.81E-02

n-Hexane (110543) NA 4.90E-01 0.00E+00 1.20E-02 3.41E-03

Hexachlorobenzene (118741) NA 4.10E-03 0.00E+00 1.00E-04 2.85E-05

Iodomethane (74884) NA 2.00E+00 0.00E+00 4.88E-02 1.39E-02

Isophorone (78591) NA 1.20E+00 0.00E+00 2.93E-02 8.35E-03

Methyl chloroform (71556) NA 6.10E-01 0.00E+00 1.49E-02 4.24E-03

Methyl methacrylate (80626) NA 1.10E+00 0.00E+00 2.68E-02 7.65E-03

Methylene chloride (75092) NA 3.60E+00 0.00E+00 8.78E-02 2.51E-02

Naphthalene (91203) 1.60E+00 6.20E-01 0.00E+00 1.51E-02 4.31E-03

Phenol (108952) 1.20E+01 3.30E+00 0.00E+00 8.05E-02 2.30E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 3.66E-04 1.04E-04

Propionaldehyde (123386) NA 1.90E+00 0.00E+00 4.63E-02 1.32E-02

Styrene (100425) NA 7.00E-01 0.00E+00 1.71E-02 4.87E-03

Tetrachloroethylene (127184) NA 4.20E-01 0.00E+00 1.02E-02 2.92E-03

Toluene (108883) NA 1.70E+00 0.00E+00 4.15E-02 1.18E-02

Vinyl acetate (108054) NA 3.10E-01 0.00E+00 7.56E-03 2.16E-03

Vinyl chloride (75014) NA 7.30E-01 0.00E+00 1.78E-02 5.08E-03

Xylenes (1330207) NA 1.26E+00 0.00E+00 3.07E-02 8.77E-03

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 3.23E-02 9.22E-03

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 9.51E-09 2.71E-09

Organic HAP Total 6.69E+01 0.00E+00 1.63E+00 4.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 1.66E+03 8.11E-02 1.16E-05

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey; CEMS data from

 Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF3_ILB

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.035 ILB COAL HEAT INPUT (10^12 BTU/YR) = 17.14

UNIT 3 RATED CAPACITY 10^6 BTU/HR 11,457

CY05 ROUTINE ILLINOIS-BASIN (ILB) SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 2.31 DATE: 07/12/06

COAL-FIRED AIR EMISSION ESTIMATES NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.444

BASED ON: ILB COAL H2O (AS-FIRED) % WT (AVG) 12.20 AIR POLLUTION CONTROL SYSTEM(S): ESPC

ILB COAL ASH (AS-FIRED) % WT (AVG) 8.60

CY05 FUEL & CEMS DATA (1) ILB COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 11,500 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

ILB TRACE-ELEMENT CONCENTRATNS (2) ILB COAL SULFUR (AS-FIRED) % WT (AVG) 2.69 PM SO2 NOx

MEDIAN EFH HAP EMISSN FACTRS (3) ILB COAL FIRED (AS-FIRED) TONS 745,146 0.11 5.4 NA

AVG OF CY01-CY05 PM STACK TEST DATA (4) ASH SPLIT TO BOTTOM % 75

VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

MEDIAN EFH HOURLY

MEDIAN ILB UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.87E+06 3.52E+04 98.12 302 403 5520 1260

PM < 10-micrometer aero. diam. (PM10_fil) NA 2.43E+05 2.39E+04 90.15 205 274 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 1.03E+05 1.27E+04 87.68 109 145 NA NA

Condensable PM (PM_cond) NA 2.39E+05 2048 2738 NA NA

Sulfur dioxide (SO2) NA 4.44E+06 4.44E+06 0.00 41376 50919 270981 61868

Nitrogen oxides (NOx) NA 1.43E+06 4.44E+05 69.04 4549 5090 NA NA

Carbon monoxide (CO) NA 2.17E+04 2.17E+04 0.00 186 249 Comparison w/ 4-28-06 LT Outputs:

Volatile organic compounds (VOC) NA 4.78E+03 4.78E+03 0.00 41.0 54.8 Air rel, lb/yr % Difference

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 1.36E+05 8.90E+04 34.55 763 1020 1,522,100 0.2

Ammonia (NH3) (6) NA 5.43E+02 5.43E-01 99.90 4.66E-03 6.22E-03

PM Trace-Element HAP

Antimony (Sb) 2.00E+00 1.53E+02 7.47E-01 99.51 6.40E-03 8.56E-03

Arsenic (As) 1.10E+01 8.40E+02 9.97E+00 98.81 8.54E-02 1.14E-01

Beryllium (Be) 2.00E+00 1.53E+02 8.34E-01 99.45 7.15E-03 9.56E-03

Cadmium (Cd) 5.00E-01 3.82E+01 1.40E+00 96.34 1.20E-02 1.60E-02

Chromium (Cr) 1.60E+01 1.22E+03 1.02E+01 99.16 8.74E-02 1.17E-01

Cobalt (Co) 3.70E+00 2.82E+02 2.07E+00 99.27 1.77E-02 2.37E-02

Lead (Pb) 1.40E+01 1.07E+03 1.24E+01 98.84 1.06E-01 1.42E-01

Manganese (Mn) 2.90E+01 2.21E+03 1.55E+01 99.30 1.33E-01 1.78E-01

Nickel (Ni) 1.90E+01 1.45E+03 1.11E+01 99.24 9.48E-02 1.27E-01

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.86E+02 5.38E+04 5.38E+04 0.00 4.61E+02 6.17E+02 922,210 0.05

Hydrogen fluoride (HF) 9.20E+01 7.40E+03 6.66E+03 10.00 5.70E+01 7.63E+01 114,080 0.008

Mercury (Hg) 8.00E-02 6.11E+00 4.72E+00 22.65 4.05E-02 5.41E-02 81.0 0.02

Selenium (Se) 1.70E+00 1.30E+02 7.14E+01 45.00 6.12E-01 8.18E-01 1,223 0.002

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 7.63E-03 1.02E-02

1,2-Dibromoethane (106934) NA 2.60E+00 2.23E-02 2.98E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 1.29E-02 1.72E-02

1,3-Dichloropropene (542756) NA 7.20E-01 6.17E-03 8.25E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 9.43E-03 1.26E-02

2-Butanone (78933) NA 3.10E+00 2.66E-02 3.55E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 1.71E-03 2.29E-03

3-Chloropropylene (107051) NA 9.10E+00 7.80E-02 1.04E-01

4-Methyl-2-pentanone (108101) NA 2.30E+00 1.97E-02 2.64E-02

4-Methylphenol (106445) NA 1.10E+00 9.43E-03 1.26E-02

Acetaldehyde (75070) NA 3.20E+00 2.74E-02 3.67E-02 54.8 -0.0005

Acetophenone (98862) NA 1.20E+00 1.03E-02 1.37E-02 20.6 0.0001

Acrolein (107028) NA 1.90E+00 1.63E-02 2.18E-02 32.6 -0.0004

Benzene (71432) NA 3.90E+00 3.34E-02 4.47E-02

Benzyl chloride (100447) NA 2.80E-01 2.40E-03 3.21E-03

Biphenyl (92524) NA 1.60E-01 1.37E-03 1.83E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 3.08E-02 4.12E-02

Bromomethane (74839) NA 8.90E-01 7.63E-03 1.02E-02

Carbon disulfide (75150) NA 1.10E+00 9.43E-03 1.26E-02

Chlorobenzene (108907) NA 1.60E-01 1.37E-03 1.83E-03

Chloroethane (75003) NA 5.30E-01 4.54E-03 6.07E-03

Chloroform (67663) NA 8.00E-01 6.86E-03 9.17E-03

Chloromethane (74873) NA 1.10E+00 9.43E-03 1.26E-02

Dibenzofuran (132649) NA 5.80E-01 4.97E-03 6.65E-03

Dibutylphthalate (84742) NA 1.10E-01 9.43E-04 1.26E-03

Dimethylphthalate (131113) NA 9.00E-02 7.71E-04 1.03E-03

Ethyl benzene (100414) NA 8.00E-01 6.86E-03 9.17E-03

Formaldehyde (50000) NA 2.60E+00 2.23E-02 2.98E-02

n-Hexane (110543) NA 4.90E-01 4.20E-03 5.61E-03

Hexachlorobenzene (118741) NA 4.10E-03 3.51E-05 4.70E-05

Iodomethane (74884) NA 2.00E+00 1.71E-02 2.29E-02

Isophorone (78591) NA 1.20E+00 1.03E-02 1.37E-02

Methyl chloroform (71556) NA 6.10E-01 5.23E-03 6.99E-03

Methyl methacrylate (80626) NA 1.10E+00 9.43E-03 1.26E-02

Methylene chloride (75092) NA 3.60E+00 3.08E-02 4.12E-02

Naphthalene (91203) 1.60E+00 6.20E-01 5.31E-03 7.10E-03

Phenol (108952) 1.20E+01 3.30E+00 2.83E-02 3.78E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 1.29E-04 1.72E-04

Propionaldehyde (123386) NA 1.90E+00 1.63E-02 2.18E-02

Styrene (100425) NA 7.00E-01 6.00E-03 8.02E-03

Tetrachloroethylene (127184) NA 4.20E-01 3.60E-03 4.81E-03

Toluene (108883) NA 1.70E+00 1.46E-02 1.95E-02

Vinyl acetate (108054) NA 3.10E-01 2.66E-03 3.55E-03

Vinyl chloride (75014) NA 7.30E-01 6.26E-03 8.36E-03

Xylenes (1330207) NA 1.26E+00 1.08E-02 1.44E-02

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 1.14E-02 1.52E-02

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 3.34E-09 4.47E-09

Organic HAP Total 6.69E+01 5.73E-01 7.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 8.48E+02 1.45E-02 9.71E-06

Notes:

(1) CY05 unit-specific total coal-burn quantities listed in Excel file "CY05 Operating Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown

 listed in Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al., along with PAF coal-region proximate coal-quality data; CEMS data from Excel file "TVA Historic

 Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05,TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF3_PRB

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.035 PRB COAL HEAT INPUT (10^12 BTU/YR) = 32.02

UNIT 3 RATED CAPACITY 10^6 BTU/HR 11,457

CY05 ROUTINE POWDER RIVER BASIN (PRB) SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 2.31 DATE: 07/12/06

COAL-FIRED AIR EMISSION ESTIMATES NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.444

BASED ON: PRB COAL H2O (AS-FIRED) % WT (AVG) 27.50 AIR POLLUTION CONTROL SYSTEM(S): ESPC

PRB COAL ASH (AS-FIRED) % WT (AVG) 5.30

CY05 FUEL & CEMS DATA (1) PRB COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 8,775 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

PRB TRACE-ELEMENT CONCENTRATNS (2) PRB COAL SULFUR (AS-FIRED) % WT (AVG) 0.35 PM SO2 NOx

MEDIAN EFH HAP EMISSN FACTRS (3) PRB COAL FIRED (AS-FIRED) TONS 1,824,322 0.11 5.4 NA

AVG OF CY01-CY05 PM STACK TEST DATA (4) ASH SPLIT TO BOTTOM % 75

VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

MEDIAN EFH HOURLY

MEDIAN PRB UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.51E+06 3.52E+04 97.67 563 403 5520 1260

PM < 10-micrometer aero. diam. (PM10_fil) NA 1.96E+05 2.39E+04 87.81 383 274 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 8.30E+04 1.27E+04 84.74 203 145 NA NA

Condensable PM (PM_cond) NA 1.00E+04 160 115 NA NA

Sulfur dioxide (SO2) NA 6.98E+05 6.98E+05 0.00 12140 7997 270981 61868

Nitrogen oxides (NOx) NA 9.69E+05 4.44E+05 54.14 5737 5090 NA NA

Carbon monoxide (CO) NA 2.85E+04 2.85E+04 0.00 456 326 Comparison w/ 4-28-06 LT Outputs:

Volatile organic compounds (VOC) NA 6.27E+03 6.27E+03 0.00 100 71.8 Air rel, lb/yr % Difference

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 4.84E+03 2.18E+03 55.00 34.9 25.0 65,007 6.9

Ammonia (NH3) (6) NA 5.43E+02 4.07E+02 25.00 6.52 4.67

PM Trace-Element HAP

Antimony (Sb) 1.50E-01 1.24E+01 1.76E-01 98.58 2.81E-03 2.01E-03

Arsenic (As) 1.20E+00 9.91E+01 1.94E+00 98.04 3.11E-02 2.23E-02

Beryllium (Be) 2.50E-01 2.07E+01 1.17E-01 99.43 1.87E-03 1.34E-03

Cadmium (Cd) 1.10E-01 9.09E+00 7.59E-01 91.64 1.22E-02 8.70E-03

Chromium (Cr) 4.30E+00 3.55E+02 5.64E+00 98.41 9.03E-02 6.47E-02

Cobalt (Co) 1.60E+00 1.32E+02 1.42E+00 98.93 2.27E-02 1.63E-02

Lead (Pb) 3.20E+00 2.64E+02 4.80E+00 98.18 7.69E-02 5.50E-02

Manganese (Mn) 1.40E+01 1.16E+03 1.19E+01 98.97 1.91E-01 1.37E-01

Nickel (Ni) 2.90E+00 2.40E+02 5.16E+00 97.84 8.27E-02 5.92E-02

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 6.90E+01 5.86E+03 1.17E+03 80.00 1.88E+01 1.34E+01 37,510 0.04

Hydrogen fluoride (HF) 5.20E+01 4.52E+03 2.26E+03 50.00 3.62E+01 2.59E+01 72,422 0.005

Mercury (Hg) 6.00E-02 4.96E+00 4.16E+00 16.14 6.66E-02 4.76E-02 133 0.02

Selenium (Se) 7.40E-01 6.11E+01 1.83E+00 97.00 2.94E-02 2.10E-02 58.7 -0.0001

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 1.42E-02 1.02E-02

1,2-Dibromoethane (106934) NA 2.60E+00 4.16E-02 2.98E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 2.40E-02 1.72E-02

1,3-Dichloropropene (542756) NA 7.20E-01 1.15E-02 8.25E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 1.76E-02 1.26E-02

2-Butanone (78933) NA 3.10E+00 4.96E-02 3.55E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 3.20E-03 2.29E-03

3-Chloropropylene (107051) NA 9.10E+00 1.46E-01 1.04E-01

4-Methyl-2-pentanone (108101) NA 2.30E+00 3.68E-02 2.64E-02

4-Methylphenol (106445) NA 1.10E+00 1.76E-02 1.26E-02

Acetaldehyde (75070) NA 3.20E+00 5.12E-02 3.67E-02 102 0.004

Acetophenone (98862) NA 1.20E+00 1.92E-02 1.37E-02 38.4 0.003

Acrolein (107028) NA 1.90E+00 3.04E-02 2.18E-02 60.8 0.003

Benzene (71432) NA 3.90E+00 6.24E-02 4.47E-02

Benzyl chloride (100447) NA 2.80E-01 4.48E-03 3.21E-03

Biphenyl (92524) NA 1.60E-01 2.56E-03 1.83E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 5.76E-02 4.12E-02

Bromomethane (74839) NA 8.90E-01 1.42E-02 1.02E-02

Carbon disulfide (75150) NA 1.10E+00 1.76E-02 1.26E-02

Chlorobenzene (108907) NA 1.60E-01 2.56E-03 1.83E-03

Chloroethane (75003) NA 5.30E-01 8.48E-03 6.07E-03

Chloroform (67663) NA 8.00E-01 1.28E-02 9.17E-03

Chloromethane (74873) NA 1.10E+00 1.76E-02 1.26E-02

Dibenzofuran (132649) NA 5.80E-01 9.28E-03 6.65E-03

Dibutylphthalate (84742) NA 1.10E-01 1.76E-03 1.26E-03

Dimethylphthalate (131113) NA 9.00E-02 1.44E-03 1.03E-03

Ethyl benzene (100414) NA 8.00E-01 1.28E-02 9.17E-03

Formaldehyde (50000) NA 2.60E+00 4.16E-02 2.98E-02 83.2 0.003

n-Hexane (110543) NA 4.90E-01 7.84E-03 5.61E-03 15.7 0.002

Hexachlorobenzene (118741) NA 4.10E-03 6.56E-05 4.70E-05

Iodomethane (74884) NA 2.00E+00 3.20E-02 2.29E-02

Isophorone (78591) NA 1.20E+00 1.92E-02 1.37E-02

Methyl chloroform (71556) NA 6.10E-01 9.77E-03 6.99E-03

Methyl methacrylate (80626) NA 1.10E+00 1.76E-02 1.26E-02

Methylene chloride (75092) NA 3.60E+00 5.76E-02 4.12E-02

Naphthalene (91203) 1.60E+00 6.20E-01 9.93E-03 7.10E-03

Phenol (108952) 1.20E+01 3.30E+00 5.28E-02 3.78E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 2.40E-04 1.72E-04

Propionaldehyde (123386) NA 1.90E+00 3.04E-02 2.18E-02

Styrene (100425) NA 7.00E-01 1.12E-02 8.02E-03

Tetrachloroethylene (127184) NA 4.20E-01 6.72E-03 4.81E-03

Toluene (108883) NA 1.70E+00 2.72E-02 1.95E-02

Vinyl acetate (108054) NA 3.10E-01 4.96E-03 3.55E-03

Vinyl chloride (75014) NA 7.30E-01 1.17E-02 8.36E-03

Xylenes (1330207) NA 1.26E+00 2.02E-02 1.44E-02

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 2.12E-02 1.52E-02

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 6.24E-09 4.47E-09

Organic HAP Total 6.69E+01 1.07E+00 7.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 8.48E+02 2.71E-02 9.71E-06

Notes:

(1) CY05 unit-specific total coal-burn quantities listed in Excel file "CY05 Operating Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown

 listed in Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al., along with PAF coal-region proximate coal-quality data; CEMS data from Excel file "TVA Historic

 Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
PAF3

PARADISE FOSSIL PLANT PARTICULATE EMISSION (TEST) LB/10^6 BTU 0.035 COAL HEAT INPUT (10^12 BTU/YR) = 49.16

UNIT 3 RATED CAPACITY 10^6 BTU/HR 11,457

CY05 ROUTINE ILB/PRB COAL-FIRED SO2 EMISSIONS (CEMS AVG) LB/10^6 BTU 2.31 DATE: 07/12/06

AIR EMISSION ESTIMATES BASED ON: NOx EMISSIONS (CEMS AVG) LB/10^6 BTU 0.444

COAL H2O (AS-FIRED) % WT (AVG) 23.06 AIR POLLUTION CONTROL SYSTEM(S): ESPC

CY05 FUEL & CEMS DATA (1) COAL ASH (AS-FIRED) % WT (AVG) 6.26

ILB/PRB TRACE-ELEMENT CONCENTRATNS (2) COAL HEAT VALUE (AS-FIRED) BTU/LB (AVG) 9,565 ALLOWABLE EMISSION RATES (LB/10^6 BTU):

MEDIAN EFH HAP EMISSN FACTRS (3) COAL SULFUR (AS-FIRED) % WT (AVG) 1.03 PM SO2 NOx

AVG OF CY01-CY05 PM STACK TEST DATA (4) COAL FIRED TONS 2,569,468 0.11 5.4 NA

ASH SPLIT TO BOTTOM % 75

STACK-EXIT SO3 CONCENTRATN PPM VOL 11.2 VOC & ORGANIC HAP CONTRL EFFCNCY (%): 0.0

MEDIAN EFH HOURLY

ILB/PRB WTD-AVG UNCONTROLLED CONTROLLED ESTIMATED EMISSIONS

TRACE-ELEMENT COAL EMISSION COAL EMISSION EFH CONTROL ANNUAL AT RATED

Pollutant/Category CONCENTRATION FACTOR FACTOR EFFICIENCY EMISSIONS CAPACITY MAX ALLOWABLE EMISSIONS

MG/KG (DRY) (2) LB/10^12 BTU LB/10^12 BTU % TONS/YR LB/HR TONS/YR LB/HR

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) NA 1.64E+06 3.52E+04 97.85 865 403 5520 1260

PM < 10-micrometer aero. diam. (PM10_fil) NA 2.13E+05 2.39E+04 88.74 588 274 NA NA

PM < 2.5-micrometer aero. diam. (PM2.5_fil) NA 8.99E+04 1.27E+04 85.91 311 145 NA NA

Condensable PM (PM_cond) NA 8.98E+04 2208 1029 QA/QC: NA NA

Sulfur dioxide (SO2) NA 2.31E+06 2.31E+06 0.00 53516 26477 0 270981 61868

Nitrogen oxides (NOx) NA 1.13E+06 4.44E+05 60.72 10286 5090 0 NA NA

Carbon monoxide (CO) NA 2.61E+04 2.61E+04 0.00 642 299

Volatile organic compounds (VOC) NA 5.75E+03 5.75E+03 0.00 141 65.9

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) NA 5.37E+04 3.25E+04 39.57 798 372

Ammonia (NH3) (6) NA 5.43E+02 2.66E+02 51.11 6.53 3.04

PM Trace-Element HAP

Antimony (Sb) 7.62E-01 6.13E+01 3.75E-01 99.39 9.22E-03 4.30E-03

Arsenic (As) 4.44E+00 3.57E+02 4.74E+00 98.67 1.17E-01 5.43E-02

Beryllium (Be) 8.29E-01 6.67E+01 3.67E-01 99.45 9.02E-03 4.21E-03

Cadmium (Cd) 2.39E-01 1.92E+01 9.82E-01 94.89 2.41E-02 1.13E-02

Chromium (Cr) 8.17E+00 6.57E+02 7.23E+00 98.90 1.78E-01 8.29E-02

Cobalt (Co) 2.29E+00 1.85E+02 1.65E+00 99.11 4.05E-02 1.89E-02

Lead (Pb) 6.77E+00 5.45E+02 7.45E+00 98.63 1.83E-01 8.53E-02

Manganese (Mn) 1.90E+01 1.53E+03 1.32E+01 99.14 3.24E-01 1.51E-01

Nickel (Ni) 8.23E+00 6.62E+02 7.22E+00 98.91 1.77E-01 8.27E-02

Gaseous Trace-Element HAP

Hydrogen chloride (HCl) 2.73E+02 2.26E+04 1.95E+04 13.52 4.80E+02 2.24E+02

Hydrogen fluoride (HF) 6.52E+01 5.53E+03 3.79E+03 31.33 9.33E+01 4.35E+01

Mercury (Hg) 6.66E-02 5.36E+00 4.36E+00 18.72 1.07E-01 4.99E-02

Selenium (Se) 1.06E+00 8.51E+01 2.61E+01 69.34 6.41E-01 2.99E-01

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) NA 8.90E-01 2.19E-02 1.02E-02

1,2-Dibromoethane (106934) NA 2.60E+00 6.39E-02 2.98E-02

1,2,4-Trichlorobenzene (120821) NA 1.50E+00 3.69E-02 1.72E-02

1,3-Dichloropropene (542756) NA 7.20E-01 1.77E-02 8.25E-03

1,4-Dichlorobenzene (106467) NA 1.10E+00 2.70E-02 1.26E-02

2-Butanone (78933) NA 3.10E+00 7.62E-02 3.55E-02

2,4-Dinitrotoluene (121142) NA 2.00E-01 4.92E-03 2.29E-03

3-Chloropropylene (107051) NA 9.10E+00 2.24E-01 1.04E-01

4-Methyl-2-pentanone (108101) NA 2.30E+00 5.65E-02 2.64E-02

4-Methylphenol (106445) NA 1.10E+00 2.70E-02 1.26E-02

Acetaldehyde (75070) NA 3.20E+00 7.86E-02 3.67E-02

Acetophenone (98862) NA 1.20E+00 2.95E-02 1.37E-02

Acrolein (107028) NA 1.90E+00 4.67E-02 2.18E-02

Benzene (71432) NA 3.90E+00 9.59E-02 4.47E-02

Benzyl chloride (100447) NA 2.80E-01 6.88E-03 3.21E-03

Biphenyl (92524) NA 1.60E-01 3.93E-03 1.83E-03

bis(2-Ethylhexyl)phthalate (117817) 6.65E-01 3.60E+00 8.85E-02 4.12E-02

Bromomethane (74839) NA 8.90E-01 2.19E-02 1.02E-02

Carbon disulfide (75150) NA 1.10E+00 2.70E-02 1.26E-02

Chlorobenzene (108907) NA 1.60E-01 3.93E-03 1.83E-03

Chloroethane (75003) NA 5.30E-01 1.30E-02 6.07E-03

Chloroform (67663) NA 8.00E-01 1.97E-02 9.17E-03

Chloromethane (74873) NA 1.10E+00 2.70E-02 1.26E-02

Dibenzofuran (132649) NA 5.80E-01 1.43E-02 6.65E-03

Dibutylphthalate (84742) NA 1.10E-01 2.70E-03 1.26E-03

Dimethylphthalate (131113) NA 9.00E-02 2.21E-03 1.03E-03

Ethyl benzene (100414) NA 8.00E-01 1.97E-02 9.17E-03

Formaldehyde (50000) NA 2.60E+00 6.39E-02 2.98E-02

n-Hexane (110543) NA 4.90E-01 1.20E-02 5.61E-03

Hexachlorobenzene (118741) NA 4.10E-03 1.01E-04 4.70E-05

Iodomethane (74884) NA 2.00E+00 4.92E-02 2.29E-02

Isophorone (78591) NA 1.20E+00 2.95E-02 1.37E-02

Methyl chloroform (71556) NA 6.10E-01 1.50E-02 6.99E-03

Methyl methacrylate (80626) NA 1.10E+00 2.70E-02 1.26E-02

Methylene chloride (75092) NA 3.60E+00 8.85E-02 4.12E-02

Naphthalene (91203) 1.60E+00 6.20E-01 1.52E-02 7.10E-03

Phenol (108952) 1.20E+01 3.30E+00 8.11E-02 3.78E-02

Polychlorinated biphenyl [PCB] (1336363) NA 1.50E-02 0.00E+00 3.69E-04 1.72E-04

Propionaldehyde (123386) NA 1.90E+00 4.67E-02 2.18E-02

Styrene (100425) NA 7.00E-01 1.72E-02 8.02E-03

Tetrachloroethylene (127184) NA 4.20E-01 1.03E-02 4.81E-03

Toluene (108883) NA 1.70E+00 4.18E-02 1.95E-02

Vinyl acetate (108054) NA 3.10E-01 7.62E-03 3.55E-03

Vinyl chloride (75014) NA 7.30E-01 1.79E-02 8.36E-03

Xylenes (1330207) NA 1.26E+00 3.10E-02 1.44E-02

Polycyclic organic matter (POM) NA 1.32E+00 0.00E+00 3.26E-02 1.52E-02

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) NA 3.90E-07 0.00E+00 9.59E-09 4.47E-09

Organic HAP Total 6.69E+01 1.64E+00 7.66E-01

pCi/gram of PM pCi/10^6 Btu Ci/yr Ci/hr

Radionuclides 53.1 8.48E+02 4.17E-02 9.71E-06

Notes:

(1) CY05 unit-specific total coal-burn quantities listed in Excel file "CY05 Operating Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown

 listed in Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al., along with PAF coal-region proximate coal-quality data; CEMS data from Excel file "TVA Historic

 Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey; ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance

 Emissions from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants

 listed as nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]).

 Criteria-pollutant emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM,

 CO & VOC) or particle-size distributions (PM10_fil & PM2.5_fil).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

INSIGNIF. BREAKER NO. 1 & 2 DUMP TRUCK UNPAVED ROAD SILT CONTENT, % 4.00 6.76 LB/VMT 100 T/HR 2.70E-01 5.41E+01 NONE 0 2.70E-01 5.41E+01

EMISSION REFUSE DISPOSAL REFUSE HAULING, FUGITIVE DUST VEHICLE SPEED, MPH 15 1000 T/YR

SOURCE ACTIVITIES ONE-WAY FULL (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 81 25 T/TRIP

NO. OF WHEELS 6 10560 FT/TRIP

WET DAYS/YR 110

DUMP TRUCK UNPAVED ROAD SILT CONTENT, % 4.00 6.74 LB/VMT 100 T/HR 2.70E-01 5.39E+01 NONE 0 2.70E-01 5.39E+01

REFUSE HAULING, FUGITIVE DUST VEHICLE SPEED, MPH 15 1000 T/YR

ONE-WAY EMPTY (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 56 25 T/TRIP

NO. OF WHEELS 10 10560 FT/TRIP

WET DAYS/YR 110

DUMP TRUCK CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 100 T/HR 8.64E-05 1.73E-02 NONE 0 8.64E-05 1.73E-02

FEED TO PILE (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1000 T/YR

EMISSIONS SUB-TOTAL 5.40E-01 1.08E+02 5.40E-01 1.08E+02

INSIGNIF. RAILCAR UNLOADER RAILCAR FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.16E-02 1.73E-01 PARTIAL 50 1.08E-02 8.64E-02

EMISSION TO SURGE HOPPER (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.51E+05 T/YR ENCLOSURE

SOURCE

SURGE HOPPER FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.16E-02 1.73E-01 ENCLOSURE 70 6.49E-03 5.18E-02

TO BC-3 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.51E+05 T/YR

EMISSIONS SUB-TOTAL 4.33E-02 3.45E-01 1.73E-02 1.38E-01

INSIGNIF. BUNKERS BC-16 , BC-17, BC--26 OR CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 5.47E-01 1.73E-01 ENCLOSURE 70 1.64E-01 5.18E-02

EMISSION BC--27 FEED TO BUNKERS (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR

SOURCE

19 TRACTOR TRUCK COAL HAULING UNPAVED ROAD SILT CONTENT, % 9.6 30.20 LB/VMT 4300 T/HR 3.20E+03 7.55E+03 WET 95 1.60E+02 3.77E+02

UNLOADING ONE-WAY FULL FUGITIVE DUST VEHICLE SPEED, MPH 20 3.64E+06 T/YR SUPPRESSION

SYSTEM (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 59.5 43 T/TRIP

NO. OF WHEELS 18 2.5 MI/TRIP

WET DAYS/YR 110

TRUCK COAL HAULING UNPAVED ROAD SILT CONTENT, % 9.6 12.30 LB/VMT 4300 T/HR 1.30E+03 3.08E+03 WET 95 6.51E+01 1.54E+02

ONE-WAY EMPTY FUGITIVE DUST VEHICLE SPEED, MPH 20 3.64E+06 T/YR SUPPRESSION

(AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 16.5 43 T/TRIP

NO. OF WHEELS 18 2.5 MI/TRIP

WET DAYS/YR 110

WATER TRUCK UNPAVED ROAD SILT CONTENT, % 9.6 25.96 LB/VMT 15 VMT/HR 6.07E+02 3.89E+02 WET 95 3.04E+01 1.95E+01

DUST SUPPRESSION DUST SUPPRESSION FUGITIVE DUST FUGITIVE DUST VEHICLE SPEED, MI/HR VEHICLE SPEED, MI/HR 15 3.12E+03 3.12E+03 HR/YR SUPPRESSION SUPPRESSION

ON HAUL ROADS (AP-42, SEC. 11.2.1) VEHICLE WEIGHT EMPTY, T 85

VEHICLE WEIGHT, T 135.04

CAPACITY, T 50.04

AVERAGE HAUL WEIGHT, T 110.02

NUMBER OF WHEELS 10

WET DAYS/YR 110

TRUCK DUMP TO BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 4300 T/HR 3.14E-01 7.43E-01 NONE 0 3.14E-01 7.43E-01

SHORT-TERM STORAGE PILE (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.64E+06 T/YR

FRONT-END LOADER UNPAVED ROAD SILT CONTENT, % 4 0.79 LB/VMT 3380 HR/YR 2.68E+00 1.59E+00 NONE 0 2.68E+00 1.59E+00

STOCKOUT/RECLAIM FUGITIVE DUST VEHICLE SPEED, MPH 2 6.76E+03 MILES/YR

AND PILE MAINT ACTIVITIES (AP-42, SEC. 11.2.1) AVG VEHICLE WEIGHT, T 90.15

NO. OF WHEELS 4

WET DAYS/YR 110

FRONT-END LOADER BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 4300 T/HR 3.14E-01 7.43E-01 NONE 0 3.14E-01 7.43E-01

FEED TO SHORT-TERM PILE (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.64E+06 T/YR

OPEN STORAGE WIND EROSION OF SILT CONTENT, % 4 2.49 LB/ACRE-D 2.1 ACRE 9.40E-01 2.15E-01 NONE 0 9.40E-01 2.15E-01

FREQ-DISTURBD PILE WET DAYS/YR 110

(EPA, 1992, SEC. 2.3.1.3.3)WIND FREQ > 12 MPH, % 7.6

FRONT-END LOADER BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 3.14E-01 3.45E-01 PARTIAL 50 1.57E-01 1.73E-01

FEED TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.64E+06 T/YR ENCLOSURE

HOPPER #1 OR #2

TRUCK HOPPER #1 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.57E-01 1.73E-01 ENCLOSURE 70 4.72E-02 5.18E-02

FEED TO BC-1 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.82E+06 T/YR

TRUCK HOPPER #2 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.57E-01 1.73E-01 ENCLOSURE 70 4.72E-02 5.18E-02

FEED TO BC-2 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.82E+06 T/YR

EMISSIONS SUB-TOTAL 5.11E+03 1.10E+04 2.60E+02 5.54E+02

Page 1 of 7
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

20 BREAKER BC-1 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.57E-01 1.73E-01 ENCLOSURE 97 4.72E-03 5.18E-03

BUILDING BREAKER NO. 1 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.82E+06 T/YR FOAM 

(BREAKERS NO. 1 & 2) SUPPRESSION

BC-2 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.57E-01 1.73E-01 ENCLOSURE 97 4.72E-03 5.18E-03

BREAKER NO. 2 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.82E+06 T/YR FOAM

SUPPRESSION

BREAKER NO. 1 PRIMARY CRUSHER --- --- 0.02 LB/T 1000 T/HR 1.82E+01 2.00E+01 ENCLOSURE 97 5.46E-01 6.00E-01

(AP-42 SEC. 8.23) 1.82E+06 T/YR FOAM

SUPPRESSION

BREAKER NO. 2 PRIMARY CRUSHER --- --- 0.02 LB/T 1000 T/HR 1.82E+01 2.00E+01 ENCLOSURE 97 5.46E-01 6.00E-01

(AP-42 SEC. 8.23) 1.82E+06 T/YR FOAM

SUPPRESSION

BREAKERS FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.57E-01 1.73E-01 ENCLOSURE 94 9.43E-03 1.04E-02

TO BC-7 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.82E+06 T/YR FOAM 1ST

CARRYOVER

BREAKERS FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.57E-01 1.73E-01 ENCLOSURE 94 9.43E-03 1.04E-02

TO BC-8 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.82E+06 T/YR FOAM 1ST

CARRYOVER

BREAKERS FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 100 T/HR 8.64E-05 1.73E-02 ENCLOSURE 94 5.18E-06 1.04E-03

BC-20 (REFUSE CONV) (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.00E+03 T/YR FOAM 1ST

CARRYOVER

BC-20 (REFUSE CONV) CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 100 T/HR 8.64E-05 1.73E-02 PARTIAL 85 1.30E-05 2.59E-03

FEED TO PILE (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.00E+03 T/YR ENCLOSURE

FOAM 2ND

CARRYOVER

EMISSIONS SUB-TOTAL 3.70E+01 4.07E+01 1.12E+00 1.23E+00

21 BREAKER BUILDING BC-3 FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.16E-02 1.73E-01 ENCLOSURE 97 6.49E-04 5.18E-03

(BREAKER NO. 3) TO BREAKER NO.3 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.51E+05 T/YR FOAM 

SUPPRESSION

BREAKER No. 3 PRIMARY CRUSHER --- --- 0.02 LB/T 1000 T/HR 2.51E+00 2.00E+01 ENCLOSURE 97 7.52E-02 6.00E-01

(AP-42 SEC. 8.23) 2.51E+05 T/YR FOAM

SUPPRESSION

BREAKER NO.3 FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.16E-02 1.73E-01 ENCLOSURE 94 1.30E-03 1.04E-02

TO BC-4 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.51E+05 T/YR FOAM 1ST

CARRYOVER

BREAKER NO.3 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 100 T/HR 4.32E-05 1.73E-02 PARTIAL 90 4.32E-06 1.73E-03

RC-1 (REFUSE CONV) (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.00E+02 T/YR ENCLOSURE

FOAM 1ST

CARRYOVER

EMISSIONS SUB-TOTAL 2.55E+00 2.04E+01 7.71E-02 6.17E-01

22 TRANSFER STN A BC-7 AND BC-8 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 3.14E-01 3.45E-01 ENCLOSURE 91 2.83E-02 3.11E-02

BC-9, BC-12, BC-19, OR BC-31 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.64E+06 T/YR FOAM 2ND

CARRYOVER

BC-45 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 3.68E-02 3.45E-01 ENCLOSURE 70 1.11E-02 1.04E-01

BC-9, BC-12 OR BC-19 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

BC-18 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 1.79E-01 3.45E-01 ENCLOSURE 94 1.07E-02 2.07E-02

BC-9 OR BC-12 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.07E+06 T/YR FOAM 1ST

CARRYOVER

SAMPLE CRUSHER SECONDRY CRUSHER --- --- 0.05 LB/T 2.55E+00 T/HR 1.16E-01 1.27E-01 ENCLOSURE 70 3.48E-02 3.82E-02

BC-7 AND BC-8 SAMPLER (AP-42, SEC. 8.23) 4.64E+03 T/YR

EMISSIONS SUB-TOTAL 6.46E-01 1.16E+00 8.49E-02 1.94E-01

23 TRANSFER BC-4 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.16E-02 1.73E-01 ENCLOSURE 91 1.95E-03 1.55E-02

STATION B BC-28 OR BC-44 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.51E+05 T/YR FOAM 2ND

CARRYOVER

BC-30 FEED TO BC-44 CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 1000 T/HR 0.00E+00 3.28E-01 ENCLOSURE 70 0.00E+00 9.83E-02

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR

BC-43A TO BC-28 CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 0.00E+00 6.56E-01 ENCLOSURE 70 0.00E+00 1.97E-01

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR

SAMPLE CRUSHER SECONDRY CRUSHER --- --- 0.05 LB/T 1.5 T/HR 9.40E-03 7.50E-02 ENCLOSURE 70 2.82E-03 2.25E-02

BC-4 SAMPLER (AP-42, SEC. 8.23) 3.76E+02 T/YR

EMISSIONS SUB-TOTAL 3.10E-02 1.23E+00 4.77E-03 3.33E-01

Page 2 of 7
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

24 OPEN LIVE BC-28 OR BC-29 FEED CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 0.00E+00 6.56E-01 PARTIAL 50 0.00E+00 3.28E-01

STORAGE PILE TO LIVE PILE NO.3 OR 4 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR ENCLOSURE

LIVE PILE No. 3 & 4

BC-28 FEED TO BC-29 CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 0.00E+00 6.56E-01 ENCLOSURE 70 0.00E+00 1.97E-01

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR

OPEN STORAGE WIND EROSION OF SILT CONTENT, % 4 2.49 LB/ACRE-D 1 ACRE 4.55E-01 1.04E-01 NONE 0 4.55E-01 1.04E-01

FREQ-DISTURBD PILE WET DAYS/YR 110

(EPA, 1992, SEC. 2.3.1.3.3)WIND FREQ > 12 MPH, % 7.6

LIVE PILE No. 3 OR 4 HOPPER CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 1000 T/HR 0.00E+00 3.28E-01 ENCLOSURE 70 0.00E+00 9.83E-02

FEED TO BC-30 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR

EMISSIONS SUB-TOTAL 4.55E-01 1.74E+00 4.55E-01 7.27E-01

25 TRANSFER STATN G BC-31 FEED TO BC-32 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 4.20E-02 3.45E-01 ENCLOSURE 88 5.05E-03 4.15E-02

OR BC-43A (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.87E+05 T/YR FOAM 3RD 

CARRYOVER

BC-43 FEED TO BC-45 OR CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 6.99E-02 6.56E-01 ENCLOSURE 70 2.10E-02 1.97E-01

TO BC-43A (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

BC-44 FEED TO CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 1000 T/HR 4.11E-02 3.28E-01 ENCLOSURE 70 1.23E-02 9.83E-02

BC-32 OR BC-45 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.51E+05 T/YR

EMISSIONS SUB-TOTAL 1.53E-01 1.33E+00 3.83E-02 3.36E-01

26 TRANSFER STATN H BC-54 AND BC-32 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 4000 T/HR 4.80E-02 6.91E-01 ENCLOSURE 97 1.44E-03 2.07E-02

BC-33, BC-35 OR BC-47 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.56E+05 T/YR FOAM 

SUPPRESSION

27 COAL STORAGE BC-33 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.10E-02 3.45E-01 ENCLOSURE 94 1.26E-03 2.07E-02

SILOS 5 & 6 STORAGE SILO #5 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.43E+05 T/YR FOAM 1ST 

CARRYOVER

BC-33 FEED TO BC-34 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.10E-02 3.45E-01 ENCLOSURE 94 1.26E-03 2.07E-02

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.43E+05 T/YR FOAM 1ST 

CARRYOVER

BC-34 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.10E-02 3.45E-01 ENCLOSURE 91 1.89E-03 3.11E-02

STORAGE SILO #6 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.43E+05 T/YR FOAM 2nd

CARRYOVER

SILOS FEED TO BC-35 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 4.20E-02 3.45E-01 ENCLOSURE 88 5.05E-03 4.15E-02

(AP-42 SEC. 11.2.3-3) (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH AVG WIND SPEED, MPH 6.85 4.87E+05 4.87E+05 T/YR FOAM 3RD FOAM 3RD

CARRYOVER

EMISSIONS SUB-TOTAL 1.05E-01 1.38E+00 9.46E-03 1.14E-01

28 TRANSFER STATN J BC-35 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 4.20E-02 3.45E-01 ENCLOSURE 85 6.31E-03 5.18E-02

FEED TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.87E+05 T/YR FOAM 4TH

BC-36 AND BC-37 CARRYOVER

BC-46 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.95E-03 3.45E-01 ENCLOSURE 70 1.79E-03 1.04E-01

FEED TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.89E+04 T/YR

BC-36 AND BC-37

EMISSIONS SUB-TOTAL 4.80E-02 6.91E-01 8.09E-03 1.55E-01

29 TRANSFER STATN K BC-36 AND BC-37 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 4.80E-02 3.45E-01 ENCLOSURE 70 1.44E-02 1.04E-01

FEED TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.56E+05 T/YR

BC-38, BC-39 AND SCREENS

BC-38 AND BC-39 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 4.80E-02 1.73E-01 ENCLOSURE 70 1.44E-02 5.18E-02

FEED TO SCREENS (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.56E+05 T/YR

(WASH PLANT)

EMISSIONS SUB-TOTAL 9.60E-02 5.18E-01 2.88E-02 1.55E-01

30 TRANSFER STATN L BC-41 FEED TO CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 6.99E-02 6.56E-01 ENCLOSURE 70 2.10E-02 1.97E-01

SURGE HOPPER (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

SURGE HOPPER CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 6.99E-02 6.56E-01 ENCLOSURE 70 2.10E-02 1.97E-01

FEED TO BC-42 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

SAMPLE CRUSHER SECONDRY CRUSHER --- --- 0.05 LB/T 1.545 T/HR 8.24E-03 7.73E-02 ENCLOSURE 70 2.47E-03 2.32E-02

BC-41 SAMPLER (AP-42, SEC. 8.23) 3.30E+02 T/YR

EMISSIONS SUB-TOTAL 1.48E-01 1.39E+00 4.44E-02 4.17E-01

31 TRANSFER STATN M BC-42 FEED TO BC-43 CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 6.99E-02 6.56E-01 ENCLOSURE 70 2.10E-02 1.97E-01

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

Page 3 of 7
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

32 BARGE UNLOADER/ BARGE UNLOADER CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 4000 T/HR 2.71E-01 6.91E-01 WATER SPRAY 80 5.43E-02 1.38E-01

SURGE HOPPER DUMP TO BC-49 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.14E+06 T/YR

BC-49 DUMP TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 4000 T/HR 2.71E-01 6.91E-01 ENCLOSURE 70 8.14E-02 2.07E-01

SURGE HOPPER (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.14E+06 T/YR

HOPPER DUMP TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.71E-01 3.45E-01 ENCLOSURE 70 8.14E-02 1.04E-01

BC-50 AND BC-51 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.14E+06 T/YR

EMISSIONS SUB-TOTAL 8.14E-01 1.73E+00 2.17E-01 4.49E-01

33 TRANSFER STATION N BC-50 & BC-51 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.71E-01 3.45E-01 ENCLOSURE 97 8.14E-03 1.04E-02

(BREAKERS NO. 4-7) BREAKERS 4-7 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.14E+06 T/YR FOAM 

SUPPRESSION

BREAKERS 4-7 PRIMARY CRUSHER --- --- 0.02 LB/T 2000 T/HR 3.14E+01 4.00E+01 ENCLOSURE 97 9.43E-01 1.20E+00

(AP-42, SEC. 8.23) 3.14E+06 T/YR FOAM

SUPPRESSION

BREAKERS FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.71E-01 3.45E-01 ENCLOSURE 94 1.63E-02 2.07E-02

TO BC-52 & BC-53 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.14E+06 T/YR FOAM 1ST

CARRYOVER

BREAKERS FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 100 T/HR 8.64E-05 1.73E-02 ENCLOSURE 94 5.18E-06 1.04E-03

REFUSE CONVEYORS (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.00E+03 T/YR FOAM 1ST

CARRYOVER

SAMPLE CRUSHER SECONDRY CRUSHER --- --- 0.05 LB/T 4.219 T/HR 1.66E-01 2.11E-01 ENCLOSURE 70 4.97E-02 6.33E-02

BC-50 & BC-51 SAMPLER (AP-42, SEC. 8.23) 6.63E+03 T/YR

REFUSE CONVEYORS CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 100 T/HR 8.64E-05 1.73E-02 PART ENCL. 85 1.30E-05 2.59E-03

FEED TO PILE (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.00E+03 T/YR FOAM 2ND

CARRYOVER

EMISSIONS SUB-TOTAL 3.21E+01 4.09E+01 1.02E+00 1.30E+00

34 TRANSFER STATN P BC-52 AND BC-53 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.71E-01 3.45E-01 ENCLOSURE 91 2.44E-02 3.11E-02

& STORAGE BYPASS FEED TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.14E+06 T/YR FOAM 2ND

BC-54 OR BC-55 CARRYOVER

BC-55 FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 1.05E-01 3.45E-01 ENCLOSURE 97 3.15E-03 1.04E-02

TO BC-55A (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.22E+06 T/YR FOAM 

(STORAGE BYPASS CONV.) SUPPRESSION

BC-55A FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 1.05E-01 3.45E-01 ENCLOSURE 94 6.30E-03 2.07E-02

BC-18 (RECLAIM CONV.) (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.22E+06 T/YR FOAM 1ST 

CARRYOVER

EMISSIONS SUB-TOTAL 4.82E-01 1.04E+00 3.39E-02 6.22E-02

35 LONG-TERM OPEN STORAGE WIND EROSION OF SILT CONTENT, % 4 2.49 LB/ACRE-D 35 ACRE 1.59E+01 3.63E+00 NONE 0 1.59E+01 3.63E+00

COAL STORAGE YARD FREQ-DISTURBD PILE WET DAYS/YR 110

(EPA, 1992, SEC. 2.3.1.3.3)WIND FREQ > 12 MPH, % 7.6

BC-19 STOCKOUT BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 1.34E-01 3.45E-01 PARTIAL 50 6.71E-02 1.73E-01

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.55E+06 T/YR ENCLOSURE

PAN SCRAPERS

BC-55 STOCKOUT BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 7.54E-02 3.45E-01 PARTIAL 95 3.77E-03 1.73E-02

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 8.73E+05 T/YR ENCLOSURE

PAN SCRAPERS FOAM 

SUPPRESSION

BC-47 STOCKOUT BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 0.00E+00 3.45E-01 PARTIAL 90 0.00E+00 3.45E-02

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR ENCLOSURE

PAN SCRAPERS FOAM 1ST

CARRYOVER

PAN SCRAPERS UNPAVED ROAD SILT CONTENT, % 4 7.60 LB/VMT 2000 T/HR 1.90E+01 2.77E+01 WET 75 4.74E+00 6.92E+00

STOCKOUT HAULING, FUGITIVE DUST VEHICLE SPEED, MPH 15 2.74E+06 T/YR SUPPRESSION

ONE-WAY FULL (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 128 52 T/TRIP

NO. OF WHEELS 4 500 FT/TRIP

WET DAYS/YR 110

PAN SCRAPERS UNPAVED ROAD SILT CONTENT, % 4 5.28 LB/VMT 2000 T/HR 1.32E+01 1.92E+01 WET 75 3.29E+00 4.80E+00

STOCKOUT HAULING, FUGITIVE DUST VEHICLE SPEED, MPH 15 2.74E+06 T/YR SUPPRESSION

ONE-WAY EMPTY (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 76 52 T/TRIP

NO. OF WHEELS 4 500 FT/TRIP

WET DAYS/YR 110

PAN SCRAPERS BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.37E-01 3.45E-01 NONE 0 2.37E-01 3.45E-01

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.74E+06 T/YR

STORAGE PILE

Page 4 of 7
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

35 LONG-TERM PAN SCRAPERS UNPAVED ROAD SILT CONTENT, % 4 7.60 LB/VMT 2000 T/HR 1.48E+01 2.77E+01 WET 75 3.71E+00 6.92E+00

(CONT'D) COAL STORAGE YARD RECLAIM HAULING, FUGITIVE DUST VEHICLE SPEED, MPH 15 2.14E+06 T/YR SUPPRESSION

(CONTINUED) ONE-WAY FULL (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 128 52 T/TRIP

NO. OF WHEELS 4 500 FT/TRIP

WET DAYS/YR 110

PAN SCRAPERS UNPAVED ROAD SILT CONTENT, % 4 5.28 LB/VMT 2000 T/HR 1.03E+01 1.92E+01 WET 75 2.57E+00 4.80E+00

RECLAIM HAULING, FUGITIVE DUST VEHICLE SPEED, MPH 15 2.14E+06 T/YR SUPPRESSION

ONE-WAY EMPTY (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 76 52 T/TRIP

NO. OF WHEELS 4 500 FT/TRIP

WET DAYS/YR 110

PAN SCRAPERS BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 1.79E-01 3.45E-01 NONE 0 1.79E-01 3.45E-01

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.07E+06 T/YR

RECLAIM HOPPER

BC-18

RECLAIM HOPPER BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 1.79E-01 3.45E-01 ENCLOSURE 97 5.37E-03 1.04E-02

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.07E+06 T/YR FOAM 

BC-18 SUPPRESSION

STORAGE PILE UNPAVED ROAD SILT CONTENT, % 4 0.45 LB/VMT 416 HR/YR 1.87E-01 8.98E-01 NONE 0 1.87E-01 8.98E-01

MAINTENANCE FUGITIVE DUST VEHICLE SPEED, MPH 2 8.32E+02 VMT/YR

DOZERS (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 40.0

NO. OF WHEELS 4

WET DAYS/YR 110

PAN SCRAPERS BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.95E-03 3.45E-01 NONE 0 5.95E-03 3.45E-01

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.89E+04 T/YR

RECLAIM HOPPER

BC-46

RECLAIM HOPPER BATCH DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.95E-03 3.45E-01 ENCLOSURE 70 1.79E-03 1.04E-01

DISCHG COAL TO (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.89E+04 T/YR

BC-46

PILE WATERING UNPAVED ROAD SILT CONTENT, % 4 1.65 LB/VMT 5 VMT/HR 8.58E+00 8.25E+00 WET 75 2.15E+00 2.06E+00

DUST SUPPRESSION FUGITIVE DUST VEHICLE SPEED, MI/HR 5 2.08E+03 HR/YR SUPPRESSION

ON HAUL ROADS (AP-42, SEC. 11.2.1) VEHICLE WEIGHT EMPTY, T 48.5

VEHICLE WEIGHT, T 90.2

CAPACITY, T 41.7

AVERAGE HAUL WEIGHT, T 69.35

NUMBER OF WHEELS 4

WET DAYS/YR 110

EMISSIONS SUB-TOTAL 8.27E+01 1.09E+02 3.31E+01 3.14E+01

36 COVERED LIVE BC-9 FEED TO SILO # 1 OR CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.47E-01 3.45E-01 ENCLOSURE 70 1.64E-01 1.04E-01

STORAGE SILOS BC-10 FEED TO SILO #2 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR

(SILOS #1 and #2)

BC-9 TO BC-10 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 2.74E-01 3.45E-01 ENCLOSURE 70 8.21E-02 1.04E-01

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.17E+06 T/YR

SILO #1or #2 TO BC-11 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.47E-01 3.45E-01 ENCLOSURE 70 1.64E-01 1.04E-01

(AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR

EMISSIONS SUB-TOTAL 1.37E+00 1.04E+00 4.11E-01 3.11E-01

37 CONDITIONERS BC-11 OR BC-12 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.47E-01 3.45E-01 ENCLOSURE 97 1.64E-02 1.04E-02

(CRUSHERS) TO SURGE HOPPER (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR FOAM 

SUPPRESSION

SURGE HOPPER TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.47E-01 3.45E-01 ENCLOSURE 94 3.28E-02 2.07E-02

CONDITIONERS (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR FOAM 1ST

CARRYOVER

CONDITIONERS SECONDARY CRUSHER --- --- 0.05 LB/T 2000 T/HR 1.58E+02 1.00E+02 ENCLOSURE 94 9.51E+00 6.00E+00

(4 WITH ONE SPARE) AP-42 SEC. 8.23 6.34E+06 T/YR FOAM 1ST

CARRYOVER

CONDITIONERS FEED CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.47E-01 3.45E-01 ENCLOSURE 91 4.93E-02 3.11E-02

TO BC-13 AND BC-14 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR FOAM 2ND

CARRYOVER

EMISSIONS SUB-TOTAL 1.60E+02 1.01E+02 9.61E+00 6.06E+00

38 POWERHOUSE BC-13 AND BC-14 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 2000 T/HR 5.47E-01 3.45E-01 ENCLOSURE 88 6.57E-02 4.15E-02

TRANSFER STATIONS BC-15, BC-17, OR BC-22 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 6.34E+06 T/YR FOAM 3RD

CARRYOVER

BC-15 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.74E-01 1.73E-01 ENCLOSURE 85 4.11E-02 2.59E-02

BC-16 OR BC-23 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.17E+06 T/YR FOAM 4TH

CARRYOVER

BC-23 OR BC-24 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.11E-01 1.73E-01 ENCLOSURE 70 3.33E-02 5.18E-02

BC-25 OR BC-27 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.28E+06 T/YR

Page 5 of 7
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

38 POWERHOUSE BC-25 TO BC-26 CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 2.22E-02 1.73E-01 ENCLOSURE 70 6.66E-03 5.18E-02

(CONT'D) TRANSFER STATIONS (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 2.57E+05 T/YR

BC-22 FEED TO CONT. DROP H2O CONTENT, % 17.4 1.73E-04 LB/T 1000 T/HR 1.11E-01 1.73E-01 ENCLOSURE 85 1.66E-02 2.59E-02

BC-24 OR BC-26 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 1.28E+06 T/YR FOAM 4TH

CARRYOVER

EMISSIONS SUB-TOTAL 1.07E+00 1.04E+00 1.63E-01 1.97E-01

39 COAL WASH PLANT FEED FROM HOPPERS CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 6.99E-02 6.56E-01 ENCLOSURE 70 2.10E-02 1.97E-01

(CLEAN COAL) T0 BC-40 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

BC-40 FEED CONT. DROP H2O CONTENT, % 11 3.28E-04 LB/T 2000 T/HR 6.99E-02 6.56E-01 ENCLOSURE 70 2.10E-02 1.97E-01

 TO BC-41 (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 4.27E+05 T/YR

MAGNETITE FEED FROM CONT. DROP H2O CONTENT, % 2 3.57E-03 LB/T 25 T/HR 1.43E-02 8.91E-02 ENCLOSURE 70 4.28E-03 2.67E-02

DELIVERY TRUCK (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 8.00E+03 T/YR

REFUSE FEED FROM WASH CONT. DROP H2O CONTENT, % 10 3.75E-04 LB/T 400 T/HR 1.04E-01 1.50E-01 ENCLOSURE 70 3.12E-02 4.50E-02

 PLANT TO REFUSE CONV. (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.56E+05 T/YR

EMISSIONS SUB-TOTAL 2.58E-01 1.55E+00 7.75E-02 4.65E-01

40 COAL WASH PLANT REFUSE CONVEYOR FEED TO BATCH DROP H2O CONTENT, % 10 3.75E-04 LB/T 400 T/HR 1.04E-01 1.50E-01 PARTIAL 50 5.21E-02 7.49E-02

COARSE REFUSE DUMP TRUCK (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.56E+05 T/YR ENCLOSURE

DISPOSAL

DUMP TRUCK UNPAVED ROAD SILT CONTENT, % 9.6 16.78 LB/VMT 400 T/HR 7.00E+01 1.01E+02 WET 95 3.50E+00 5.04E+00

REFUSE HAULING ON FUGITIVE DUST VEHICLE SPEED, MPH 15 5.56E+05 T/YR SUPPRESSION

HAUL ROAD (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 85 50 T/TRIP

ONE-WAY FULL NO. OF WHEELS 6 0.75 MI/TRIP

WET DAYS/YR 110

DUMP TRUCK UNPAVED ROAD SILT CONTENT, % 0 0.00 LB/VMT 400 T/HR 0.00E+00 0.00E+00 NONE 0 0.00E+00 0.00E+00

REFUSE HAULING ON FUGITIVE DUST VEHICLE SPEED, MPH 15 5.56E+05 T/YR

REFUSE PILE (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 85 50 T/TRIP

ONE-WAY FULL NO. OF WHEELS 6 0.35 MI/TRIP

WET DAYS/YR 110

DUMP TRUCK BATCH DROP H2O CONTENT, % 10 3.75E-04 LB/T 400 T/HR 1.04E-01 1.50E-01 NONE 0 1.04E-01 1.50E-01

DISCHARGE TO PILE (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 5.56E+05 T/YR

DOZER SPREADING DOZER SPREADING UNPAVED ROAD UNPAVED ROAD SILT CONTENT, % SILT CONTENT, % 0 0.00 LB/VMT 3120 HR/YR 0.00E+00 0.00E+00 0.00E+00 0.00E+00 NONE 0 0.00E+00 0.00E+00 0.00E+00 0.00E+00

COARSE REFUSE FUGITIVE DUST VEHICLE SPEED, MPH 2 6.24E+03 VMT/YR

(AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 40

NO. OF WHEELS 4

WET DAYS/YR 110

OPEN STORAGE WIND EROSION OF SILT CONTENT, % 0 0.00 LB/ACRE-D 40 ACRE 0.00E+00 0.00E+00 NONE 0 0.00E+00 0.00E+00

FREQ-DISTURBD PILE WET DAYS/YR 110

(EPA, 1992, SEC. 2.3.1.3.3)WIND FREQ > 12 MPH, % 7.6

DUMP TRUCK UNPAVED ROAD SILT CONTENT, % 0 0.00 LB/VMT 400 T/HR 0.00E+00 0.00E+00 NONE 0 0.00E+00 0.00E+00

REFUSE HAULING ON PILE FUGITIVE DUST VEHICLE SPEED, MPH 15 5.56E+05 T/YR

ONE-WAY EMPTY (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 35 50 T/TRIP

NO. OF WHEELS 6 0.35 MI/TRIP

WET DAYS/YR 110

DUMP TRUCK UNPAVED ROAD SILT CONTENT, % 9.6 9.02 LB/VMT 400 T/HR 3.76E+01 1.02E-02 WET 95 1.88E+00 5.12E-04

REFUSE HAULING ON FUGITIVE DUST VEHICLE SPEED, MPH 15 5.56E+05 T/YR SUPPRESSION

HAUL ROAD (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 35 50 T/TRIP

ONE-WAY EMPTY NO. OF WHEELS 6 0.75 MI/TRIP

WET DAYS/YR 110

EMISSIONS SUB-TOTAL 1.08E+02 1.01E+02 5.53E+00 5.26E+00

CY05 PAF SOLID-FUEL-HANDLING SYSTEM PARTICULATE-MATTER (PM) EMISSION TOTALS:

UNCONTROLLED TSP CONTROLLED TSP

T/YR LB/HR T/YR LB/HR

POINT-SOURCE 0.00E+00 0.00E+00 0.00E+00 0.00E+00

FUGITIVE 5.54E+03 1.16E+04 3.13E+02 7.13E+02

------------ ------------ ------------ ------------

5.54E+03 1.16E+04 3.13E+02 7.13E+02

Page 6 of 7
coal

Table 4-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 SOLID-FUEL-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION PM SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

NOTES:

References

(1) The sources of emission equations/factors are:

(a) Material drop operations (continuous and batch) EPA, AP-42, 4th Edition, Section 11.2.3, 1988

(b) Unpaved roads EPA, AP-42, 4th Edition, Section 11.2.1, 1988

(c) Coal crushers, primary and secondary (high-moisture material) EPA, AP-42, 4th Edition, Section 8.23, 1982

(d) Wind erosion from active (frequently disturbed) piles EPA, Fugitive Dust Background Document and Technical Information Document for Best Available Control Measures, 1992.

(2) The sources for meteorological input parameters are:

(a) Average wind speed (6.85 mph) and frequency of winds greater than 12 mph (7.6 %) Paradise Fossil Plant Meteorological Tower, 1985-86 Data Base

(b) Number of wet days per year (110) National Weather Service, Paducah, Kentucky Airport Data, 1984-94 Average

(3) The sources of control efficiencies are:

(a) Wet suppression (haul road fugitive dust) 75-95 %(AWMA, Air Pollution Engineering Manual, p. 143-144, 1992)

(b) Water spray (barge unloader) 80 % (DOE/RG/10312-1 (Vol. 2), Technical Guide for Estimating Fugitive Dust Impacts from Coal Handling Operations, p. 4-3, 1984)

(c) Enclosure of conveyors and transfer points 70% (AWMA, Air Pollution Engineering Manual, p. 794, 1992)

(d) Foam suppression 90% (AWMA, Air Pollution Engineering Manual, p. 794, 1992)

(e) Foam suppression - 1st carryover 80% Engineering Estimate

(f) Foam suppression - 2nd carryover 70% Engineering Estimate

(g) Foam suppression - 3rd carryover 60% Engineering Estimate

(h) Foam suppression - 4th carryover 50% Engineering Estimate

(i) Partial enclosure 50% Engineering Estimate

*Reference: CY05 Particulate-Matter (PM) Emission Estimates (expressed as Total Suspended Particulates [TSP]), adapted** from 12-3-96 Title V Permit Application for Paradise Fossil Plant (PAF).

TVA Environmental Technologies

** Reference: Excel file "Coal and Limestone Handled in CY 2005.xls" in 2-3-06 e-mail from S.L. Priddy to C.M. Anderson et al. 07/12/06

Page 7 of 7
Lstone

Table 5-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 LIMESTONE- AND LIME-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES*

EMISSION EMISSION APPLICABLE INPUT PARAMETERS (2) UNCONTROLLED CONTROLLED 

UNIT UNIT EMISSION SCALING FACTOR PM EMISSIONS % CONTROL PM EMISSIONS

NUMBER DESCRIPTION COMPONENT EQUATION (1) PARAMETER VALUE EMISSION FACTOR (PROCESS MEASURE) T/YR LB/HR CONTROLS EFFICIENCY(3) T/YR LB/HR

41 LIMESTONE RAIL/ TRUCK LIMESTONE UNPAVED ROAD SILT CONTENT, % 9.6 11.5 LB/VMT 900 T/HR 2.48E+02 1.18E+03 WET 95 1.24E+01 5.90E+01

TRUCK UNLOADING HAULING ONE-WAY EMPTY FUGITIVE DUST VEHICLE SPEED, MPH 20 3.79E+05 T/YR SUPPRESSION

SYSTEM (AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 15 25 T/TRIP

NO. OF WHEELS 18 2.85 MI/TRIP

WET DAYS/YR 110

TRUCK LIMESTONE UNPAVED ROAD SILT CONTENT, % 9.6 22.9 LB/VMT 900 T/HR 4.94E+02 2.35E+03 WET 95 2.47E+01 1.17E+02

HAULING ONE-WAY FULL FUGITIVE DUST VEHICLE SPEED, MPH 20 3.79E+05 T/YR SUPPRESSION

(AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 40 25 T/TRIP

NO. OF WHEELS 18 2.85 MI/TRIP

WET DAYS/YR 110

DISCHARGE FROM CONT. DROP H2O CONTENT, % 3.1 1.93E-03 LB/T 900 T/HR 3.66E-01 1.74E+00 NONE 0 3.66E-01 1.74E+00

RAILCAR/TRUCK (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.79E+05 T/YR

TO HOPPER

EMISSIONS SUB-TOTAL 7.42E+02 3.53E+03 3.75E+01 1.78E+02

42 RECLAIM/RECEIVING BAGFILTER --- MANUFACTURER'S --- 2.00E-02 GR/SCF 3600 SCF/MIN 2.70E+02 6.17E+01 BAG FILTER 99 2.70E+00 6.17E-01

HOPPER FEEDER VENT INFORMATION: OUTLET PER VENT

BAGFILTER (DC-1) GRAIN LOADING 1 COLLECTR

8760 HR/YR

43-44 TRANSFER STATION BAGFILTER --- MANUFACTURER'S --- 2.00E-02 GR/SCF 3700 SCF/MIN 5.56E+02 1.27E+02 BAG FILTER 99 5.56E+00 1.27E+00

BAGFILTERS VENTS INFORMATION: OUTLET PER VENT

(DC-2A, 2B) GRAIN LOADING 2 COLLECTRS

8760 HR/YR

45 LIMESTONE STORAGE BAGFILTER --- MANUFACTURER'S --- 2.00E-02 GR/SCF 2000 SCF/MIN 1.50E+02 3.43E+01 BAG FILTER 99 1.50E+00 3.43E-01

SILO BIN VENT FILTER VENT INFORMATION: OUTLET PER VENT

(DC-3) GRAIN LOADING 1 COLLECTR

8760 HR/YR

46-48 LIMESTONE STORAGE BAGFILTER --- MANUFACTURER'S --- 2.00E-02 GR/SCF 4000 SCF/MIN 9.01E+02 2.06E+02 BAG FILTER 99 9.01E+00 2.06E+00

SILO VIBRATING FEEDER VENTS INFORMATION: OUTLET PER VENT

BAGFILTERS (DC-4A, 4B, 4C) GRAIN LOADING 3 COLLECTRS

8760 HR/YR

49-51 LIMESTONE PREP BLDG DISCHARGE FROM CONT. DROP H2O CONTENT, % 3.1 1.93E-03 LB/T 720 T/HR 3.66E-01 1.39E+00 ENCLOSURE 70 1.10E-01 4.17E-01

CONVEYORS N-306-A,-B, & -C (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.79E+05 T/YR

Page 1 of 2

CONVEYORS N-306-A,-B, & -C (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 3.79E+05 T/YR

TO SURGE HOPPERS

52 LIMESTONE HANDLING DISCHARGE TO STORAGE CONT. DROP H2O CONTENT, % 3.1 1.93E-03 LB/T 900 T/HR 0.00E+00 1.74E+00 TELESCOPING 50 0.00E+00 8.69E-01

BULK STORAGE PILE PILE FROM CONVEYOR (AP-42 SEC. 11.2.3-3) AVG WIND SPEED, MPH 6.85 0.00E+00 T/YR CHUTE

OPEN STORAGE WIND EROSION OF SILT CONTENT, % 5 3.12E+00 LB/ACRE-D 4.00 ACRE OF 2.27E+00 5.19E-01 NONE 0 2.27E+00 5.19E-01

FREQ-DISTURBD PILE WET DAYS/YR 110 DISTURBED

(EPA, 1992, SEC 2.3.1.3.3)WIND FREQ > 12 MI/HR, % 7.6 PILE AREA

LIMESTONE RECLAIM UNPAVED ROAD SILT CONTENT, % 5 9.12E-01 LB/VMT 2 VMT/HR 7.59E-01 1.82E+00 NONE 0 7.59E-01 1.82E+00

(BULLDOZER) FUGITIVE DUST VEHICLE SPEED, MI/HR 2 832 HR/YR

(AP-42, SEC. 11.2.1) VEHICLE WEIGHT, T 80

NUMBER OF WHEELS 4

WET DAYS/YR 110

EMISSIONS SUB-TOTAL 3.03E+00 4.08E+00 3.03E+00 3.21E+00

53-54 LIME STORAGE SILO BAGFILTER --- ENG. ESTIMATE --- 2.00E-02 GR/SCF 1150 SCF/MIN 1.38E+00 3.94E+01 BAG FILTER 99 1.38E-02 3.94E-01

BAGFILTERS VENTS OUTLET PER VENT

GRAIN LOADING 2 COLLECTRS

70 HR/YR

PAF LIMESTONE/LIME HANDLING SYSTEMS PARTICULATE-MATTER (TSP) EMISSION TOTALS:

UNCONTROLLED TSP CONTROLLED TSP

T/YR LB/HR T/YR LB/HR

POINT-SOURCE 1.88E+03 4.68E+02 1.88E+01 4.68E+00

ON-PERMIT FUGITIVES 3.76E+00 7.21E+00 3.51E+00 5.37E+00

OFF-PERMIT FUGITIVES 7.42E+02 3.53E+03 3.71E+01 1.76E+02

FUGITIVE TOTAL 7.46E+02 3.53E+03 4.06E+01 1.82E+02

------------ ------------ ------------ ------------

Page 1 of 2 ON-PERMIT TOTAL 1.88E+03 4.75E+02 2.23E+01 1.00E+01
Lstone

Table 5-2. PARADISE FOSSIL PLANT (PAF): ACTUAL CY05 LIMESTONE- AND LIME-HANDLING PARTICULATE-MATTER (PM) EMISSION ESTIMATES* (Cont'd)

NOTES:

References

(1) The sources of emission equations/factors are:

(a) Material drop operations (continuous and batch) EPA, AP-42, 4th Edition, Section 11.2.3, 1988

(b) Unpaved roads EPA, AP-42, 4th Edition, Section 11.2.1, 1988

(c) Wind erosion from active (frequently disturbed) piles EPA, Fugitive Dust Background Document and Technical Information Document for Best Available Control Measures,1992.

(d) Bagfilter outlet grain loading Manufacturer's Information

(2) The sources for meteorological input parameters are:

(a) Average wind speed (6.85 mph) and frequency of winds greater than 12 mph (7.6 %) Paradise Fossil Plant Meteorological Tower, 1985-86 Data Base

(b) Number of wet days per year (110) National Weather Service, Paducah, Kentucky Airport Data, 1984-94 Average

(3) The sources of control efficiencies are:

(a) Telescoping chute on stockout 50% (Engineering Estimate)

(b) Bagfilter >99% (Manufacturer's Information)

(c) Wet suppression (for haul roads) 95 % (AWMA, Air Pollution Engineering Manual, p. 143-144, 1992)

(d) Enclosure of conveyors and transfer points 70% (AWMA, Air Pollution Engineering Manual, p. 794, 1992)

*Reference: CY05 Particulate-Matter (PM) Emission Estimates (expressed as Total Suspended Particulates [TSP]), adapted** from 12-3-96 Title V Permit Application for Paradise Fossil Plant (PAF).

TVA Environmental Technologies

** Reference: 1-22-04 Conference Call between J.W. Osborne, B.L. Barnard, & J.D. Lokey (& subsequent voice mail from J.W. Osborne). 07/12/06

Page 2 of 2
ash

Paradise Fossil Plant (PAF) Ash Handling*

Process Description:

Bottom ash (slag) flows from the furnaces into slag tanks equipped with clinker grinders underneath that crush the 

slag into smaller particles. Fly ash collected in the economizer hoppers falls into a Denslury pot (water-impounded

tub) from which it is sluiced to the slag tanks. The wet slurry in the slag tanks is sluiced by Jetpulsion pumps to the

slag pond. Fugitive dust emissions from the powerhouse portion of the slag handling system are judged to be

negligible since it is wet and completely enclosed. The mixture of bottom ash and economizer ash is reclaimed

from the slag pond using a front-end loader and stacked in the dewatering area. After the ash has sufficiently

dewatered, it is loaded out to trucks using a front-end loader and hauled offsite for use in the customer's process.

In addition, the customer has been recovering previously disposed slag in a mining/processing operation located

elsewhere on the PAF reservation. This facility is completely separate from PAF operations, and no emission

estimates for this facility were included in the 12-3-96 Title V permit application.

Fly ash collected in gas-duct, air-preheater, and electrostatic-precipitator (ESP) hoppers is evacuated by hydroveyors.

The hydroveyors use water to create a vacuum & move the ash and conveying air to air separator tanks. The water

and ash mix in the tanks to form a wet slurry, while the conveying air (with a negligible dust loading) is vented to the

atmosphere. The wet slurry drains by gravity to the fly ash pond. Once the fly ash is placed in the active ash pond,

it remains wet and is generally submerged under a layer of water. Fugitive dust emissions from fly ash disposal

are judged to be negligible.

Ash Tonnage Estimates:

The maximum potential bottom ash/economizer ash (slag) production was estimated in the Title V permit application

based on maximum boiler heat input capacities, minimum heating value for coal, maximum percent ash, & maximum

potential operation, using the typical fly ash/bottom ash split for cyclone-fired boilers & the typical split for fly ash

capture between the economizer & ESP, as shown below:

U 1-3

Maximum boiler heat input capacity, 10^6 Btu/unit-hr = 25375

Minimum heat content for coal, Btu/lb = 1.10E+04

Maximum coal ash content, % = 15

Cyclone boiler fly ash/bottom ash split, % fly ash = 25

Economizer hopper capture of fly ash, % = 10

Potential max. slag production (dry), tons/yr (tpy) = 1.17E+06

Fugitive Dust Emission Estimates & Controlled Emission Factors (EF):

Fugitive dust emissions due to slag reclaim haul roads, pile maintenance, and wind erosion of open storage areas,

were estimated in the Title V permit application (Table 6-2) for these slag handling quantities as:

Loaders hauling slag from pond to dewatering area, tons/yr (tpy) = 2.20E-01

Loaders dumping slag at dewatering area, tpy = 4.62E-02

Slag reclaim loader traffic in dewatering area, tpy = 1.37E-01

Loaders dumping slag in haul trucks, tpy = 6.11E-01

Open storage wind erosion (dewatering area), tpy = 1.14E-01

Haul vehicles--one-way (full) travel departing plant site, tpy = 1.71E+01

Haul vehicles--one-way (empty) return traffic on plant site, tpy = 1.50E+01

Bottom/econ. ash disposal fugitive dust emission total, tpy = 3.32E+01

Bottom/econ. ash disposal fugitive dust EF, lb/dry ton = 5.65E-02

Title V Total Ash Handling PM Emission Estimate, tpy = 3.32E+01

PAF Gypsum Handling*

Process Description:

Gypsum is formed in the wet flue-gas-desulfurization (FGD) scrubbers of PAF Units 1 and 2 as limestone reacts with

sulfur dioxide (SO2). Since the FGD scrubbers also serve as the principal particulate matter (PM) emission control

devices for PAF Units 1 and 2, the scrubber effluent slurry contains fly ash as well as gypsum. The gypsum slurry

exits the scrubbers via gravity overflow to an effluent slurry tank (one per unit), from which it is pumped to the highest

point of the rim ditch system. Rim ditches convey the slurry (pumped at about 15% solids) to 1 of 2 settling ponds

(or stacking cells). The rim ditches are constructed from dewatered gypsum already deposited in the stacking area.

As a stacking cell is filled, incoming slurry is diverted to the other cell, and the first cell is allowed to dewater. Then

a hydraulic trackhoe is used to excavate some of the dewatered gypsum, forming a higher rim-ditch wall to allow for

additional sluicing capacity. After the gypsum is excavated, it is spread and formed using a track dozer.

Page 1 of 4
ash

Side-slope soil cover may be added as needed to the gypsum stack using onsite soil. Pan scrapers are used for 

soil transport, and a dozer is used to spread the soil cover. Pile capping activities had not yet begun at the time

of the Title V permit application, but emissions from these activities were included in the application to cover the

possibility of their beginning during this permit cycle. Soil for pile capping will also be obtained onsite.

Gypsum and Cover Material Tonnage Estimates:

Maximum annual gypsum production was estimated for the Title V permit application using maximum boiler heat input

capacity for PAF Units 1-2, maximum SO2 levels in the flue gases entering the FGD scrubbers (5.4 lb/10^6 Btu,

based on the SO2 permit limit for PAF Unit 3--at that time all 3 units burned the same compliance coal), nominal

maximum scrubber SO2 removal efficiency (88%), continuous annual operation (8760 hr/yr), 5% unreacted limestone

(LS) in the gypsum slurry, and an estimated 15% inerts (fly ash + LS inerts) in the gypsum slurry. The maximum

annual wet gypsum excavation rate was calculated using the estimated maximum annual gypsum production, the

estimated percentage of gypsum production that is used for rim-ditch formation (15%), and the estimated moisture

content of the excavated gypsum (50%). Maximum cover material (soil) usage was also estimated.

U 1-2

Maximum boiler heat input capacity, 10^6 Btu/unit-hr = 6959

Number of scrubbed units = 2

Maximum SO2 level entering the FGD scrubbers, lb/10^6 Btu = 5.4

Molecular weight of SO2, lb/lb-mole = 64.06

Nominal maximum scrubber SO2 removal efficiency, % = 88

Gypsum (CaSO4.2H2O) : SO2 stoichiometric molar ratio = 1

Molecular weight of CaSO4.2H2O, lb/lb-mole = 172.2

Unreacted LS (CaCO3) in gypsum slurry, % = 5

Molecular weight of CaCO3, lb/lb-mole = 100.1

Estimated inert content of gypsum slurry, % = 15

Maximum annual gypsum production rate (dry), tons/yr (tpy) = 9.43E+05

Estimated fraction of gypsum production used in rim ditch, % = 15

Estimated moisture content of excavated gypsum, % = 50

Maximum annual gypsum excavation rate (wet), tpy = 2.83E+05

Maximum annual soil cover material, cubic yards/yr = 3.70E+04

Soil cover material bulk density, ton/cubic yard = 1.49

Maximum annual soil cover material usage, tpy = 5.51E+04

Fugitive Dust Emission Estimates & Controlled Emission Factors (EF):

Fugitive dust emissions due to trackhoe excavation, pile maintenance and wind erosion of gypsum open storage areas,

along with soil cover material hauling, were estimated in the 12-3-96 Title V permit application (Table 7-2) as follows:

Gypsum Stacking:

Rim ditch formation--trackhoe excavation, tpy = 2.78E-04

Rim ditch formation--trackhoe movement, tpy = 6.76E-02

Pile maintenance (dozer), tpy = 2.34E-01

Open storage wind erosion, tpy = 9.10E+00

Gypsum stacking fugitive dust emission total, tpy = 9.40E+00

Gypsum stacking fugitive dust EF, lb/dry ton gypsum productn = 1.99E-02

Cover Material Usage:

Cover matl haul--one-way (full) travel on unpaved roads, tpy = 5.10E-01

Cover material haul--one-way (full) travel over pile, tpy = 3.58E+00

Cover material haul--one-way (empty) travel over pile, tpy = 2.09E+00

Cover matl haul--one-way (empty) travel on unpaved roads, tpy = 2.98E-01

Pile maintenance/capping (dozer), tpy = 1.26E+00

Cover material fugitive dust emission total, tpy = 7.74E+00

Cover material fugitive dust EF, lb/ton = 2.81E-01

Title V Total Gypsum Handling PM Emission Estimate, tpy = 1.71E+01

*Reference: Title V Permit Application, Paradise Fossil Plant, 12-3-96.

Note: Due to the de minimis exemption for Toxics Release Inventory (TRI) reporting, trace-element components of fugitivedust emissions from cover-material usage are not considered in TRI estimates. Only trace-element components of byproducthandling (ash, gypsum) PM emissions are considered to be subject to TRI reporting requirements. 

Page 2 of 4
ash

CY05 PAF By-Product Handling Fugitive-Dust Emission Estimates

CY05 PAF By-Product (Ash/Gypsum) Production/Utilization Estimates**

Production, tons/yr (tpy) Notes

Fly Ash (U1-2) = 85,479

Fly Ash (U3) = 40,193

Fly Ash Total = 125,672

Bottom Ash/Slag = 377,016

Gypsum (U1-2) = 508,926

Production Subtotal = 1,011,614

Utilization, tpy

Fly Ash = 0

Bottom Ash/Slag = 337,203 Off-Site Processing for Roofing Granules, Blasting Grit

0 On-Site for Road Construction and Repair

Bottom Ash/Slag Total = 337,203

Gypsum = 113,523 On-Site Cover material for coal wash refuse

3,158 Off-Site Agricultural Soil Amendment

0

0

Gypsum Total = 116,681

Utilization Subtotal = 453,884

**Reference: Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

 E.C. Miller confirmed that all production & utilization quantities are dry basis in her 2-28-00 e-mail to J.D. Lokey.

Note: CY05 PAF ash/gypsum production estimates are based on 75% boiler slag/25% fly ash split

Gypsum estimates are based on methodology provided by I.J. Berty.

CY05 PAF By-Product Handling Particulate-Matter (PM)/Fugitive Dust Emission Estimates

PM Emissions,

tons/yr (tpy) Notes:

PAF Ash-Handling Point Sources = Negligible

PAF Bottom Ash/Slag Handling = Negligible

PAF Gypsum Handling = 5.07E+00

PAF Bottom Ash/Slag Byproduct Sales = 9.52E+00

PAF Fly Ash Byproduct Disposal = Negligible

CY05 PAF By-Product Handling PM Emission Total = 1.46E+01 For sources subject to TRI reporting.

CY05 PAF By-Product Handling Trace-Element PM/Fugitive-Dust Emission Estimates, tpy***

PAF Total Byproduct-Handling

Point Gypsum Bottom Fly Ash Trace-Element PM/Fugitive

Element Sources Handling Ash Sales Disposal Emissions, tpy

Antimony (Sb) - 7.34E-05 3.26E-05 - 1.06E-04

Arsenic (As) - 3.44E-04 8.48E-05 - 4.29E-04

Barium (Ba) - 1.49E-03 7.60E-03 - 9.10E-03

Beryllium (Be) - 4.45E-05 2.94E-05 - 7.39E-05

Cadmium (Cd) - 2.62E-05 2.55E-05 - 5.17E-05

Chromium (Cr) - 3.04E-04 8.72E-04 - 1.18E-03

Cobalt (Co) - 2.18E-04 5.50E-04 - 7.68E-04

Copper (Cu) - 2.88E-04 3.74E-04 - 6.62E-04

Lead (Pb) - 5.50E-04 1.71E-04 - 7.21E-04

Manganese (Mn) - 4.28E-04 3.26E-03 - 3.69E-03

Mercury (Hg) - 1.02E-06 3.01E-06 - 4.03E-06

Molybdenum (Mo) - 2.76E-04 4.04E-04 - 6.81E-04

Nickel (Ni) - 3.00E-04 7.71E-04 - 1.07E-03

Selenium (Se) - 4.89E-05 7.56E-05 - 1.24E-04

Silver (Ag) - 1.60E-06 1.41E-05 - 1.57E-05

Thallium (Tl) - 5.91E-05 5.79E-05 - 1.17E-04

Vanadium (V) - 9.33E-04 3.65E-03 - 4.58E-03

Page 3 of 4
ash

Zinc (Zn) - 1.39E-03 1.04E-03 - 2.43E-03

***Reference: PISCES Model (ver. 3.11) outputs, obtained from 3-11-02 P31 file on "envshr" drive .

Note: Emission estimates were not included for chloride (Cl) and fluoride (F) since the TRI-reportable form of these

elements are the acid gas compounds hydrochloric acid (HCl) aerosol & hydrogen fluoride (HF). The Cl & F anion

concentrations estimated for the pyrite, bottom ash, fly ash & gypsum solids streams are believed to exist as 

neutralized salts of HCl & HF (and therefore are not TRI reportable).

Polycyclic Aromatic Compounds (PAC) and Hydrocarbons (PAH) in Coal Fly Ash and Bottom Ash 

Pollutant (CAS No.) Coal Fly Ash (mg/kg) Coal Bottom Ash (mg/kg)

Frequency Frequency

EPCRA PAC of Detection Median Average of Detection Median Average

Benz(a)anthracene (56-55-3) 3/15 1.00E-04 1.95E-04 6/20 7.91E-04 1.42E-03

Benzo(a)phenanthrene (218-01-9) 17/30 3.00E-04 7.15E-04 11/24 7.50E-03 7.12E-03

Benzo(a)pyrene (50-32-8) 1/16 2.50E-05 6.57E-05 8/23 1.71E-03 3.55E-03

Benzo(b)fluoranthene (205-99-2) 1/14 4.00E-04 4.00E-04 1/14 1.98E-02 1.88E-02

Benzo(k)fluoranthene (207-08-9) 1/11 5.00E-04 5.00E-04 1/14 2.17E-02 2.15E-02

Dibenz(a,h)anthracene (53-70-3) 1/16 2.50E-05 3.47E-05 8/22 7.67E-04 3.73E-03

Fluoranthene (206-44-0) 21/34 1.80E-03 2.88E-02 12/28 3.39E-03 7.11E-03

Indeno(1,2,3-cd)-pyrene (193-39-5)2/14 5.86E-03 6.16E-03 6/20 9.26E-04 3.57E-03

Other EPCRA PAH

Anthracene (120-12-7) 5/15 5.00E-04 7.45E-04 5/19 6.86E-04 1.17E-03

Benzo(g,h,i)perylene (191-24-2) 1/16 2.50E-05 6.07E-05 6/21 1.48E-03 1.53E-03

Naphthalene (91-20-3) 30/42 7.10E-02 2.98E-01 21/29 1.80E-02 3.90E-02

Phenanthrene (85-01-8) 25/38 1.30E-02 1.57E-01 15/27 1.10E-02 1.52E-02

** **Reference: 5-29-01 e-mail from N. Goodman (EPRI) to J.D. Lokey.

[Data obtained from EPRI's PISCES Database, Individual Data Points for Trace Components in Combustion Byproducts--

All coal types, all USGS provinces, all boiler types, excluding poor or unknown quality data; concentrations are dry basis]

Non-detect concentrations are set = to 0.5 x detection limit (DL), excluding samples where DL are > 2 x the highest quantified value.

No data are available for PAC/PAH concentrations in gypsum byproducts.

CY05 PAF 1-3 Ash-Handling PAC/PAH PM/Fugitive-Dust Emission Estimates, tpy***

PAF Total Ash-Handling

Point Bottom Fly Ash PAC/PAH PM/Fugitive

Pollutant (CAS No.) Sources Ash Sales Disposal Emissions, tpy

EPCRA PAC

Benz(a)anthracene (56-55-3) - 7.53E-09 - 7.53E-09

Benzo(a)phenanthrene (218-01-9) - 7.14E-08 - 7.14E-08

Benzo(a)pyrene (50-32-8) - 1.63E-08 - 1.63E-08

Benzo(b)fluoranthene (205-99-2) - 1.88E-07 - 1.88E-07

Benzo(k)fluoranthene (207-08-9) - 2.07E-07 - 2.07E-07

Dibenz(a,h)anthracene (53-70-3) - 7.30E-09 - 7.30E-09

Fluoranthene (206-44-0) - 3.23E-08 - 3.23E-08

Indeno(1,2,3-cd)-pyrene (193-39-5) - 8.81E-09 - 8.81E-09

Other EPCRA PAH

Anthracene (120-12-7) - 6.53E-09 - 6.53E-09

Benzo(g,h,i)perylene (191-24-2) - 1.40E-08 - 1.40E-08

Naphthalene (91-20-3) - 1.71E-07 - 1.71E-07

Phenanthrene (85-01-8) - 1.05E-07 - 1.05E-07 TVA Air, Land & Water Sciences

07/12/06

Page 4 of 4
NH3

Data Elements Needed Input value

Plant Configuration APH, Wet FGD, No FGC PAF Unit 1 PAF Unit 2 PAF Units 1-2 PAF Unit 3

Total coal burn (tons/yr): (4)

 1,866,460 2,127,618 3,994,078 2,569,468

Total boiler use (hr/yr): (4)

 7,397 8,452 15,848 5,705

Flue gas flow by CEMS or by amount of coal burned (2) Hours of NH3 feed (hr/yr): (5)

 3,185 3,811 6,996 3,072

CY05 SCR operating factor (w/ NH3 feed): 0.431 0.451 0.441 0.538

Coal burn (tons/ozone season) ILB 1,741,886 Coal burn during SCR NH3 feed (tons/yr): 803,715 959,356 1,763,070 1,383,648

PRB 21,184

Coal heating value (Btu/lb) (3) ILB 11500 Region PAF Unit 1 PAF Unit 2 PAF Units 1-2 PAF Unit 3

PRB 8775 ILB 1,847,875 2,098,385 3,946,260 745,146

PRB 18,585 29,233 47,818 1,824,322

NOx Reduction Ammonia Slip Dry Basis Total 1,866,460 2,127,618 3,994,078 2,569,468

Average ammonia slip (ppmv wet basis) (6) 1.8383 2 ppmvd (6) at 3 % O2.

Operating factor for SCR/SNCR (fraction) (7) 1 Region PAF Unit 1 PAF Unit 2 PAF Units 1-2 PAF Unit 3

ILB 795,712 946,174 1,741,886 401,258

FGC Ammonia Injection PRB 8,003 13,181 21,184 982,390

Total 803,715 959,356 1,763,070 1,383,648

Fly Ash Sales Factor (decimal fraction) (8) 0 NH3 rcvd lbs

988,000 (truck) Truck-unloading NH3 emission factor = 1.38E-05 lb/lb of recpts

Fugitive losses from tank farm (9) 15.6 18,800,924 (rail) Railcar-unloading NH3 emission factor = 1.05E-07 lb/lb of recpts

Ammonia in boiler water treatment (lbs) (10)

 10,374 44,460 lbs of aqua ammonia, assumed to be 35% ammonia

Boiler water discharge (open tank or ash pond) Ash Pond

Notes:

(1) Ammonia RY2005 Release Calculator model (v0.3) based on "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," by S.L. Wilson, K.E. Harrison, & L.S. Monroe.

(2) The model estimates flue-gas flow from coal-burn quantity using bituminous coal-fired wet flue-gas F factor at 3% O2 (12,423 wet std. ft^3/MBtu)

(3) Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey (PAF Units 1-2) & Excel file "CY 2005 TRI Coal Data_020306.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. (PAF Unit 3).

(4) Excel file "CY05 Operating Statistics from DataFuser (012306).xls" in FPG Env Affr - TRI folder on "Chapgfs5" server.

(5) SCR hours with ammonia feed provided in the TRI CY05 Fossil Questionnaire and archived in CY 05\Completed Questionnaires\PAF folder. 

(6) TRI team decided to use vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours, per 1-11-01 conversation with R.A. Babb, unless recent flue-gas measurements are available. 

 To convert dry-basis flue-gas concentration to wet-basis, multiply by ratio of bituminous coal-fired F-factors at 0% O2: 9,780/10,640 (dry std. ft^3/MBtu)/(wet std. ft^3/MBtu).

 O2 content or total air in flue gas where slip was measured must be considered to estimate mass emissions from ammonia slip concentration. Since the NH3 estimator model

 requires NH3 concentration expressed at 3% O2, adjust the measured NH3 value from measured O2 level to 3% O2 by multiplying by (20.9-3)/(20.9-measured %O2).

(7) Since the coal burn has been adjusted for the hours of SCR operation, the operating factor is 1.0

(8) No CY05 PAF fly-ash sales, per Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al., archived in the CY 05\Release Estimates\Ash Data folder.

(9) Anhydrous ammonia receipts/usage listed in 3-13-06 e-mail from K.J. Dukes to M.F. Broder et al., archived in CY 05\Completed Questionnaire\PAF folder. 

 Fugitives from tank farm are included in only the first model run for PAF Units 1 and 2. 

(10) Aqua NH3 usage listed in 3-13-06 e-mail from K.J. Dukes to M.F. Broder et al., archived in CY05\Completed Questionnaire\PAF folder. 

 Unless otherwise indicated, BWT NH3 usage estimated at aqua NH3 concentratn = 35 weight %. Aqua usage was split equally among the three units. 

PAF U1-2 NH3 PAF NH3 Stack Emissions, lb/yr

Species Type of Release ILB PRB Total Contrl Effcncy, % PAF 1 PAF 2

NH3 SCR-exit 40,420 375 40,795

NH3 Stack 0.40 2.81 3.22 99.99 1.47 1.75

Ammonium salts (1) Stack 1,139 2.82 1,142

NH3 Fugitive 7,292 335 7,627

Notes:

(1) Stack releases of ammonium salts such as ammonium bisulfate (ABS) and ammonium sulfate (AS), expressed as NH3-equivalent mass rates, are emitted in the particulate-matter (PM) phase.

 They are subsumed within stack PM emissions for emission-inventory purposes, and also are not reportable for Toxics Release Inventory (TRI) purposes.

TVA Environmental Technologies

07/12/06

Table 1. Input Data for CY05 PAF Units 1-2 Ammonia (NH3) Emission-Estimation Model (1) 

PAF Units 1-2 NH3/ABS Air Emissions, lb/yr

Coal Region

Table 2. Summary of CY05 PAF Units 1-2 Ammonia (NH3) & Ammonium-Salt Air Emission Estimates

CY05 PAF Units 1-3 Coal Burn & Boiler/SCR Operating Data:

CY05 PAF Units 1-3 Coal Burn by Supply Region, tons/yr (3)

CY05 PAF Units 1-3 Coal burned by region during NH3 feed, tons/yr

Page 1 of 1
H2SO4

CY05 Paradise Fossil Plant (PAF) Sulfuric Acid (H2SO4) Manufacture/Emission Estimates

Sulfuric acid (H2SO4) is created in the ductwork downstream of coal-fired boilers by the combination of water vapor and sulfur trioxide (SO3).

Most of the coal sulfur is released during combustion as sulfur dioxide (SO2), but a portion is further oxidized to form SO3. A paper by Hardman,

Stacy, & Dismukes [HSD] as revised (1) is incorporated in EPRI's Lark-Tripp (LT) emission-estimation model that is used by many electric utilities for

Toxics Release Inventory (TRI) reporting. The HSD study indicates that for a given boiler type (e.g., cyclone-fired) and coal type (e.g., Eastern

bituminous), the SO3:SO2 molar ratio can be considered constant. Data in the HSD paper (see "Inputs" worksheet) indicate that cyclone-fired

boiler-exit SO3 concentrations are 1.6 % of the SO2 concentrations for Eastern bituminous coals, and 0.3 % for Powder

River Basin (PRB) subbituminous coal. The PAF boilers are cyclone-fired. In CY05, PAF Units 1-2 burned nearly 100% Illinois Basin (ILB)

Easten bituminous coal, but CY05 PAF Unit 3 heat inputs consisted of 34.9 % ILB coal & 65.1 % PRB subbituminous

coal. PAF Units 1-3 flue-gas measurements(2) have indicated that boiler-exit SO3/H2SO4 flue-gas concentrations produced when burning 100%

ILB coal are about 40 parts per million by volume dry-basis (ppmvd) at 3% flue-gas oxygen (O2) concentration, whereas burning

an equal mix of ILB and PRB coals in PAF Unit 3 produced about 5 ppmvd boiler-exit SO3/H2SO4 concentrations.

At high proportions of low-sulfur PRB coal burned in PAF Unit 3, SO3 concentrations may be too low for proper operation of the

electrostatic precipitator (ESP), the particulate-matter (PM) emission control system for PAF 3. Molten sulfur (S) may be burned

in a flue-gas conditioning (FGC) system, producing SO3 for injection into the boiler flue gas downstream of the air heater (AH). 

At flue-gas temperatures prevailing at & downstream of the AH, essentially all the SO3 combines with water vapor to form H2SO4.

SO3/H2SO4 adsorb onto & react with fly ash particles, decreasing their resistivity so as to enhance PM removal efficiency in the ESP.

No molten S was burned in the FGC system during CY05; the system was inactive. (3)

Table 1. CY05 PAF Flue-Gas-Conditioning (FGC) SO3/H2SO4 Manufacture Estimates

CY05 PAF molten-S receipts 0 pounds Molten-S tank capacity = 50 tons

CY05 PAF molten S burned 0.00 tons

FGC SO3/H2SO4 production 0 tons H2SO4 equivalent/yr (based on sulfur receipts)

Boiler-produced and other SO3/H2SO4 concentrations can be reduced by PM-control devices (e.g., ESP), SO2 removal systems (e.g.,

flue-gas desulfurization (FGD) scrubbers), and other equipment (e.g., air heaters). Some H2SO4 condenses on AH surfaces where

it may react with the metal to form salts, and some adsorbs onto & reacts with flue-gas fly-ash particles. Similarly, H2SO4 collected

along with the ash in a cold-side ESP or bagfilter may react with the ash to form salts. Scrubbers will typically neutralize all of the

H2SO4 captured. H2SO4 captured in air heaters and emission control equipment was considered to be neutralized by reaction with

metal surfaces or alkaline components of the ash or scrubber slurry and will not be reported as a TRI release. Nominal H2SO4 control

efficiencies in these equipment (as listed in the HSD study) were used to estimate CY05 PAF SO3/H2SO4 emissions.

Table 2. CY05 PAF Coal-fired Region-Specific Boiler Combustion-Derived SO3/H2SO4 Manufacture/Emission Estimates (HSD Method)

COAL REGION: IL Basin Bituminous BOILER/COAL TYPE: CYCL/E. BITUM SO3/SO2 MOLAR RATIO (%): 1.6

Blr Unit: PAF 1 PAF 2 PAF 3 PAF 1-3

Coal Burned, tons/year 1,847,875 2,098,385 745,146 4,691,406

Coal Heating Value, As Received (Btu/lb) 11,500 11,500 11,500

Sulfur Content, % 2.69 2.69 2.69

Coal Sulfur Conversion to Sulfur Oxides (SOx), % 95 95 95

Coal-fired Heat Inputs, 10^12 Btu/yr 42.50 48.26 17.14 107.90

Boiler-Exit SOx expressed as SO2, tons/yr 94,349 107,139 38,046 239,534

Boiler-Exit SOx converted to SO3, % 1.60 1.60 1.60

Boiler SO3/H2SO4 Production, tons H2SO4/yr 2,311 2,624 932 5,867

Air Pollution Control System(s): AH/HSE+WV AH/HSE+WV AH/HSE+ESP

Overall SO3/H2SO4 Control Efficiency, % 44.8 44.8 34.6

Boiler contributn to SO3/H2SO4 stack emssn, tons H2SO4/yr 1277 1450 610 3,337

COAL REGION: PRB Subbituminous BOILER/COAL TYPE: CYCL/PRB SO3/SO2 MOLAR RATIO (%): 0.3

Blr Unit: PAF 1 PAF 2 PAF 3 PAF 1-3

Coal Burned, tons/year 18,585 29,233 1,824,322 1,872,140

Coal Heating Value, As Received (Btu/lb) 8,775 8,775 8,775

Sulfur Content, % 0.35 0.35 0.35

Coal Sulfur Conversion to Sulfur Oxides (SOx), % 87.5 87.5 87.5

Coal-fired Heat Inputs, 10^12 Btu/yr 0.33 0.51 32.02 32.86

Boiler-Exit SOx expressed as SO2, tons/yr 114 179 11,163

Boiler-Exit SOx converted to SO3, % 0.300 0.300 0.300

Boiler SO3/H2SO4 Production, tons H2SO4/yr 0.522 0.822 51.3 52.6

Air Pollution Control System(s): AH/W+WV AH/W+WV AH/W+ESP

Overall SO3/H2SO4 Control Efficiency, % 41.5 41.5 55.0

Boiler contributn to SO3/H2SO4 stack emssn, tons H2SO4/yr 0.306 0.481 23.1 23.9

Page 1 of 4
H2SO4

Table 3. CY05 PAF Coal-Fired Boiler-Total Combustion-Derived SO3/H2SO4 Manufacture/Emission Estimates (HSD Method)

Blr Unit: PAF 1 PAF 2 PAF 1-2 PAF 3 PAF 1-3

Coal-Total Heat Inputs, 10^12 Btu/yr 42.83 48.78 91.60 49.16 140.76

Boiler-Exit SOx expressed as SO2, tons/yr 94,463 107,318 201,781 49,208 250,989

Boiler SO3/H2SO4 Production, tons H2SO4/yr 2,312 2,625 4,937 983 5,920

Boiler contributn to SO3/H2SO4 stack emssn, tons H2SO4/yr 1277 1450 2,728 633 3,361

SO3/H2SO4 Control Efficiency, % 44.7 44.7 44.7 35.6 43.2

Blr contrib. to SO3/H2SO4 stk concen (ppmvd at 3 % O2) 20.6 20.5 20.5 8.9 16.5

Production & Emission Estimates for SO3/H2SO4 Derived from PAF Selective-Catalytic-Reduction (SCR) Reactors

Ammonia (NH3)-based selective-catalytic-reduction (SCR) reactors for nitrogen oxides (NOx) control have been installed on PAF Units 1-3 

since CY00. A side reaction in the SCR catalyst produces additional SO3, with design oxidation rates (4) of 0.75 % of SO2 input

to the SCR being converted to SO3. Total CY05 SCR in-service hours (with & without NH3 inputs) (5) were used to estimate annual emissions.

An additional complexity related to the SCR operation is the gas-phase reaction between NH3 inputs and excess flue-gas SO3/H2SO4.

Wilson et al. (6) indicate that NH3, an alkaline chemical, is quite reactive with SO3/H2SO4 at flue-gas conditions existing at and downstream

of the AH (temperatures 257 deg F and cooler). NH3 slip (NH3 escaping the SCR catalytic chamber) will neutralize some of the flue-gas

SO3/H2SO4 to form ammonium salts. Ammonium bisulfate (NH4HSO4) is expected to be the predominant product when SO3 is present in

excess of NH3 concentrations, whereas ammonium sulfate ([NH4]2SO4) is expected to predominate when NH3 is more than double the SO3

concentration. The vendor-guaranteed maximum SCR-exit NH3 slip (at 20,000 hours SCR operation) is 2 ppmv dry basis. (7) As

noted in Table 7, PAF SCR-exit (AH-inlet) flue-gas SO3/H2SO4 concentrations are predicted to exceed maximum NH3 levels. Reaction with

NH3 slip should proceed very nearly to completion, consuming essentially all the NH3 slip to form NH4HSO4 solid particles that will be effectively 

captured by the PM control systems. The contribution of SCR reactors to PAF SO3/H2SO4 emissions was estimated (per HSD study) as:

SCR releases = (production - NH3 neutralization)*(1 - control efficiency/100)

Table 4. CY05 PAF Coal-fired Region-Specific SCR-Derived SO3/H2SO4 Manufacture/Emission Estimates (HSD Method)

COAL REGION: IL Basin Bituminous Blr Unit: PAF 1 PAF 2 PAF 1-2 PAF 3 PAF 1-3

Boiler-Exit SOx expressed as SO2, tons/yr 94,349 107,139 201,488 38,046 239,534

SCR total (w/ & w/o NH3) in-service hours 3,586 4,133 3,400

Boiler in-service hours 7,397 8,452 5,705

SCR operation factor (total) 0.485 0.489 0.596

SCR SO3/H2SO4 production, tons H2SO4/yr 525 602 1,127 260 1,387

Air Pollution Control System(s): AH/HSE+WV AH/HSE+WV AH/HSE+ESP

Overall SO3/H2SO4 Control Efficiency, % 44.8 44.8 34.6

SCR-outlet NH3 Slip (ppmvd at 3 % O2) 2 2 2

SCR in-service hours (with NH3) 3,185 3,811 3,072

SCR operation factor (with NH3) 0.431 0.451 0.538

SCR contributn to SO3/H2SO4 stack emssn, tons H2SO4/yr 261 297 558 153 711

COAL REGION: PRB Subbituminous Blr Unit: PAF 1 PAF 2 PAF 1-2 PAF 3 PAF 1-3

Boiler-Exit SOx expressed as SO2, tons/yr 114 179 293 11,163 11,455

SCR total (w/ & w/o NH3) in-service hours 3,586 4,133 3,400

Boiler in-service hours 7,397 8,452 5,705

SCR operation factor (total) 0.485 0.489 0.596

SCR SO3/H2SO4 production, tons H2SO4/yr 0.633 1.00 1.64 76.4 78.0

Air Pollution Control System(s): AH/W+WV AH/W+WV AH/W+ESP

Overall SO3/H2SO4 Control Efficiency, % 41.5 41.5 55.0

SCR-outlet NH3 Slip (ppmvd at 3 % O2) 2 2 2

SCR in-service hours (with NH3) 3,185 3,811 3,072

SCR operation factor (with NH3) 0.431 0.451 0.538

SCR contributn to SO3/H2SO4 stack emssn, tons H2SO4/yr 0.132 0.194 0.326 11.8 12.2

Table 5. CY05 PAF Coal-Fired Boiler-Total SCR-Derived SO3/H2SO4 Manufacture/Emission Estimates (HSD Method)

Blr Unit: PAF 1 PAF 2 PAF 1-2 PAF 3 PAF 1-3

Coal-Total Heat Inputs, 10^12 Btu/yr 42.83 48.78 91.60 49.16 140.76

Total-Coal SCR SO3/H2SO4 Production, tons H2SO4/yr 526 603 1,128 337 1,465

SCR contributn to SO3/H2SO4 stack emssn, tons H2SO4/yr 261 298 559 165 723

SO3/H2SO4 Control Efficiency, % 50.4 50.6 50.5 51.1 50.6

SCR contrib. to SO3/H2SO4 stk concen (ppmvd at 3 % O2) 4.2 4.2 4.2 2.3 3.5

Page 2 of 4
H2SO4

Production & Emission Estimates for SO3/H2SO4 Derived from PAF Unit 3 Flue-Gas Conditioning (FGC) System

The HSD method for estimating SO3/H2SO4 manufactured by FGC systems is based on expected SO3 flue-gas concentrations and an

FGC operating factor (fraction of coal burn when FGC system operates). The default SO3 concentration for FGC systems with injection

after the APH is 5 ppmv, but 10 ppmv is the operational concentration for the PAF Unit 3 FGC system. (8) The FGC system has not been

operated since CY02. The CY02 coal-burn fraction during FGC system operation was estimated by setting the quantity of FGC SO3/H2SO4

manufacture (as predicted by the HSD method) equal to the amount of H2SO4 predicted to result from burning CY02 sulfur (S) receipts.

The HSD paper indicates that release of SO3/H2SO4 manufactured in FGC systems varies according to coal type and SO3 injection 

location. The PAF Unit 3 FGC system SO3 injection point is downstream of the air heaters (AH).(8) HSD control efficiencies are:

ESP FGC SO3/H2SO4 removal for injection dnstrm of AH = 90 % for E. bitum. coal & 98 % for W. bitum & subitum coals.

Table 6. CY05 PAF Flue-Gas-Conditioning (FGC) SO3/H2SO4 Manufacture/Emission Estimates (HSD Method)

CY05 Parameters: PAF 3

Coal Region IL Basin PRB All Coals

Coal Burn, ton/yr (as received) 745,146 1,824,322 2,569,468

Heat Value, Btu/lb (as received) 11,500 8,775

FGC System Operating Factor, % 0.00 0.00 Based on CY05 S receipts.

SO3 Injection Rate, ppmv at 6% O2 10 10

FGC SO3/H2SO4 production, tons H2SO4/yr 0 0 0

SO3/H2SO4 release due to FGC operatn, tons/yr 0.0 0.0 0.0

Table 7. CY05 Estimates of Coal-fired SO3/H2SO4 Manufactured in PAF Boilers + FGC & SCR Production (HSD Method)

AH-Inlet SO3/H2SO4 Flue-Gas Concentrations & Mass Rates

Blr Unit: PAF1 PAF2 PAF 1-2 PAF3 PAF 1-3

SO3/H2SO4 Production Rate, tons H2SO4/yr 2,837 3,228 6,065 1,320 7,385

AH-inlet SO3/H2SO4 Concentration (ppmvd at 3 % O2) 45.7 45.6 45.7 18.5 36.2

Table 8. CY05 PAF Coal-fired SO3/H2SO4 Emission Estimates (HSD Method)

Stack-Exit SO3/H2SO4 Flue-Gas Concentrations & Emission Rates

Blr Unit: PAF1 PAF2 PAF 1-2 PAF3 PAF 1-3

SO3/H2SO4 Stack Emissions, tons H2SO4/yr 1,538 1,748 3,286 798 4,084

Overall SO3/H2SO4 Control Efficiency, % 45.8 45.8 45.8 39.6 44.7

Stack-exit SO3/H2SO4 Concentration (ppmvd at 3 % O2) 24.8 24.7 24.7 11.2 20.0

A test campaign (9) was conducted on PAF Unit 2 in March 2005 to evaluate opacity-reduction measures such as hydrated-lime injection.

Stack-exit SO3/H2SO4 flue-gas measurements averaged 17.7 ppmvd at 3% O2 under baseline conditions (burning 100% ILB coal,

with in-service SCR reactors but no lime injection). Stack-exit SO3/H2SO4 flue-gas measurements burning ILB coal with sulfur content typical

of CY05 coal burn, but with the SCR reactors bypassed and no lime injection, were reported as 14.2 ppmvd at 3% O2. This value

closely matches PAF Units 1-2 ILB stack-exit SO3/H2SO4 flue-gas measurements(2) prior to SCR installation, about 13 ppmvd at 3% O2.

TVA considers these limited SO3/H2SO4 stack data, although less than those predicted by the HSD method (Table 8), to be reasonably

representative of CY05 PAF Units 1-2 emissions, and has decided to use the test data for those units' TRI and emission-fee inventory estimates.

CY05 PAF Units 1-2 SO3/H2SO4 emissions were estimated in Table 9 based on annual-average stack-exit flue-gas concentrations, as

apportioned from the test data according to each unit's CY05 SCR operation factor. HSD emission estimates were deemed appropriate for

PAF Unit 3, with its high fraction of low-sulfur PRB coal burn. No AH-inlet SO3/H2SO4 flue-gas measurements were made in the March 2005

campaign. AH-outlet flue-gas concentrations were measured, but these data are not considered representative for predicting SO3/H2SO4

manufacture in PAF boilers and SCR reactors. Due to relatively low AH-outlet temperatures (duct averages ranged from 280 - 309 degrees F),

an unquantified extent of SO3/H2SO4 reduction may be expected to occur across the AH. TVA believes that the HSD-method predictions

in Table 7 are realistic values for AH-inlet mass rates and annual-average flue-gas concentrations, and will use those values to estimate

PAF boiler and SCR-reactor SO3/H2SO4 manufacture and treatment quantities for TRI reporting.

Table 9. CY05 PAF Coal-fired SO3/H2SO4 Emission Estimates (Final Values)

Stack-Exit SO3/H2SO4 Flue-Gas Concentrations & Emission Rates

Blr Unit: PAF1 PAF2 PAF 1-2 PAF3 PAF 1-3

Stack-exit SO3/H2SO4 Concentration (ppmvd at 3 % O2) 15.9 15.9 15.9 11.2 14.3

SO3/H2SO4 Stack Emissions, tons H2SO4/yr 988 1126 2,114 798 2,912

Overall SO3/H2SO4 Control Efficiency, % 65.2 65.1 65.1 39.6 60.6

Page 3 of 4
H2SO4

Notes:

(1) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented

 at US DOE-FETC Conference on Formation, Distribution, Impact, & Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, 3-98;

 revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid Emissions from Coal-Fired Power

 Plants"); and by L.S. Monroe, 5-01, and by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total

 Sulfuric Acid Emissions from Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating

 Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(2) Per 4-27-99 personal communication between G.T. Munson and J.D. Lokey. 

(3) Per 1-10-06 e-mail from J.E. Perkins to C.M. Anderson, no sulfur burn occurred at PAF in CY05.

(4) Per 3-19-03 e-mail from R.A. Babb to S.S. Koss et al., confirmed in 2-15-05 e-mail from J.D. Giles to C.M. Anderson.

(5) SCR hours with & w/o ammonia feed listed in PAF TRI CY05 Fossil Questionnaire, archived in CY 05\Completed Questionnaires\PAF folder.

(6) S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05.

(7) Per 1-11-01 conversation with R.A. Babb regarding vendor-guaranteed maximum SCR-exit NH3 slip at 20,000 hours SCR operation.

(8) Per 4-18-03 phone conversation between J.H. Lytle and J.D. Lokey.

(9) Word file "PAF U2 Opacity Reduction Testing Final Report1.doc," 4-8-05, authored by M.A. Thompson, downloaded 5-25-05 from

 TVA Fossil Power Group (FPG) Air, Gas, Water, & Yard (AGWY) Systems' SO3 Mitigation website (TVA Intranet).

TVA Environmental Technologies

07/12/06

Page 4 of 4
welding

Table 1. Paradise Fossil Plant (PAF) - CY05 Welding Rod Emissions

Type Description Emission Factor 1,2 Emissions (lbs)

Allied FGD Total Cr Co Mn Ni Pb PM10 Cr Co Mn Ni Pb PM10

14Mn- 4Cr 0 0 0 13.9 ND 232 17.1 ND 81.6 0.00 0.00 0.00 0.0

AVERAGE 2,966 5,262 8,228 3.46 0.01 15.68 2.72 0.93 18.37 2.85 0.01 12.90 2.24 0.77 151.1

E110 0 0 0 0.02 ND 20.2 1.12 ND 20.8 0.00 0.00 0.00 0.0

E11018 0 0 0 9.69 ND 13.8 1.02 ND 57.0 0.00 0.00 0.00 0.0

E308 456 414 870 5.24 0.01 3.46 1.84 ND 10.8 0.46 0.00 0.30 0.16 9.4

E310 30 0 30 25.3 ND 22 1.96 0.24 15.1 0.08 0.07 0.01 0.00 0.5

E316 36 0 36 9.7 ND 5.9 0.93 ND 10.0 0.03 0.02 0.00 0.4

E410 10 0 10 ND ND 6.85 0.14 ND 13.2 0.01 0.00 0.1

E6010 2,150 0 2,150 0.03 ND 9.91 0.04 ND 25.6 0.01 2.13 0.01 55.0

E6011 0 0 0 0.05 0.01 9.98 0.05 ND 38.4 0.00 0.00 0.00 0.00 0.0

E6012 0 0 0 ND ND ND ND ND 8.0 0.0

E6013 10 0 10 0.04 0.01 9.45 0.02 ND 19.7 0.00 0.00 0.01 0.00 0.2

E7018 9,660 1,068 10,728 0.06 0.01 10.3 0.02 ND 18.4 0.06 0.01 11.05 0.02 197.4

E7024 200 0 200 0.01 ND 6.29 ND ND 9.2 0.00 0.13 1.8

E7028 0 0 0 0.13 ND 8.46 ND 1.62 18.0 0.00 0.00 0.00 0.0

E70S 0 0 0 0.01 0.01 3.18 0.01 ND 5.2 0.00 0.00 0.00 0.00 0.0

E70T 0 0 0 0.04 ND 8.91 0.05 ND 15.1 0.00 0.00 0.00 0.0

E71T 0 0 0 0.02 0.02 6.62 0.04 ND 12.2 0.00 0.00 0.00 0.00 0.0

E8018 1,240 0 1,240 0.17 ND 0.3 0.51 ND 17.1 0.02 0.04 0.06 21.2

E9015 0 0 0 ND ND ND ND ND 17.0 0.0

E9018 220 0 220 2.12 ND 7.83 0.13 ND 16.9 0.05 0.17 0.00 3.7

ECoCr 0 0 0 ND ND ND ND ND 27.9 0.0

EM12K 0 0 0 ND ND ND ND ND 0.05 0.0

ENi-Cl 0 0 0 ND ND 0.39 8.9 ND 18.2 0.00 0.00 0.0

ENiCrMo 0 104 104 4.2 ND 0.43 2.47 ND 11.7 0.04 0.00 0.03 1.2

ENi-Cu 0 0 0 ND ND ND ND ND 10.1 0.0

Welding Rod Usage (lbs) 3

ENi-Cu 0 0 0 ND ND ND ND ND 10.1 0.0

ENi-Cu-2 0 0 0 ND ND 2.12 4.23 ND ND 0.00 0.00

ER1260 0 0 0 0.04 ND ND ND ND 20.5 0.00 0.0

ER316 0 0 0 5.28 ND 2.45 2.26 ND 3.2 0.00 0.00 0.00 0.0

ER5154 0 0 0 0.1 ND 0.34 ND ND 24.1 0.00 0.00 0.0

ERNiCrMo 0 0 0 3.53 ND 0.7 12.5 ND 3.9 0.00 0.00 0.00 0.0

ERNiCu 0 0 0 0.01 ND 0.22 4.51 ND 2.0 0.00 0.00 0.00 0.0

Total 16,978 6,848 23,826 -- -- -- -- -- -- 3.60 0.02 26.83 2.53 0.77 442.1

Notes:

1

 Emission Factors: Pounds (lb) of metal (trace-element hazardous air pollutant [HAP]) emitted per 10,000 lb of welding rods used, or lb of particulate-matter < 10 micrometers (PM-10) per 1000 lb of welding rods

 used (from AP-42, 5th Edition, Section 12.19 Electric Arc Welding, 1/95, Table 12.19-1 and 19-2, selecting the highest emission factor for a given electrode where multiple welding processes are listed).

2 ND denotes "No Data."

3

 CY05 PAF welding-rod consumption data taken from Excel file "Fossil Fugitive Air Emissions CY05.xls" posted 4-26-06 in FPG Env Affr - TRI folder on "Chapgfs5" server.

Welding-rod emissions were not subsumed in PAF plant-total fugitive air emissions, but are included in this file to document that emissions from PAF welding activities are negligible.

TVA Environmental Technologies

07/12/06

Page 1 of 1
air

PARADISE FOSSIL PLANT

BOILERS + FUGITIVE SOURCES

CY05 AIR EMISSION ESTIMATES DATE: 07/12/06

(TONS/YEAR) BASED ON:

CY05 FUEL & CEMS DATA (1) Paradise Fossil Plant (PAF) Air Emission Estimates, tons/year

REGION-SPECIFIC TRACE ELEM (2)

MEDIAN EFH HAP EMISSN FACTORS (3) Unit 1 Unit 2 Unit 3 Boiler Total Other Sources & Plant Total

AVG OF CY01-CY05 PM STACK TEST DATA (4) Coal-fired Alternate Alt_fuel as Coal-fired Alternate Coal-fired Alternate Coal-fired Alternate Alt_fuel, % Coal Limestone By-Product Fugitive PAF Fugitive, %

+ SCR Fuels Total % of Total + SCR Fuels Total + SCR Fuels Total + SCR Fuels Total Blr Total Handling Handling Handling Total Total PAF Total

Criteria/Non-HAP Pollutants

Filterable particulate matter (PM_fil) 1525 0.137 1526 0.009 1684 0.0450 1684 865 0.180 865 4074 0.362 4075 0.01 313 59.4 22.3 394 4469 8.8

PM < 10-micrometer aero. diam. (PM10_fil) 1037 0.0758 1037 0.007 1145 0.0225 1145 588 0.0942 588 2770 0.192 2771 0.007 Not Not Not 2771

PM < 2.5-micrometer aero. diam. (PM2.5_fil) 549 0.0169 549 0.003 606 0.00562 606 311 0.0224 311 1467 0.0449 1467 0.003 Estimated Estimated Estimated 1467

Condensable PM (PM_cond) 428 0.0877 428 0.02 488 0.0292 488 2208 0.116 2208 3124 0.233 3124 0.007 3124

Sulfur dioxide (SO2) 13561 1.98 13563 0.01 17319 0.639 17320 53516 3.02 53519 84396 5.65 84402 0.007 84402

Nitrogen oxides (NOx) 11464 1.68 11466 0.01 14124 0.540 14125 10286 2.21 10289 35874 4.43 35879 0.01 35879

Carbon monoxide (CO) 467 0.378 467 0.08 532 0.112 532 642 0.488 643 1641 0.979 1642 0.06 1642

Volatile organic compds (VOC) 103 0.0217 103 0.02 117 0.00450 117 141 0.0261 141 361 0.0522 361 0.01 361

Sulfuric acid (SO3/H2SO4) as H2SO4 (5) 988 0.0942 988 0.01 1126 0.0314 1126 798 0.125 798 2912 0.251 2912 0.01 2912

Ammonia (NH3) (6) 7.35E-04 7.35E-04 0.0 8.74E-04 8.74E-04 6.53 6.53 6.53 6.53 0.0 6.14 12.7 48.5

Trace-Element HAP

Antimony (Sb) 2.48E-02 2.06E-04 2.50E-02 0.8 2.76E-02 6.85E-05 2.77E-02 9.22E-03 2.73E-04 9.49E-03 6.16E-02 5.47E-04 6.22E-02 0.9 1.07E-03 4.23E-05 1.06E-04 1.21E-03 6.34E-02 1.9

Arsenic (As) 3.86E-01 3.74E-05 3.86E-01 0.01 4.27E-01 1.25E-05 4.27E-01 1.17E-01 4.96E-05 1.17E-01 9.30E-01 9.94E-05 9.31E-01 0.01 2.29E-03 8.23E-05 4.29E-04 2.80E-03 9.33E-01 0.3

Beryllium (Be) 3.86E-02 2.80E-05 3.86E-02 0.07 4.23E-02 9.35E-06 4.23E-02 9.02E-03 3.72E-05 9.06E-03 8.99E-02 7.46E-05 9.00E-02 0.08 3.54E-04 8.82E-06 7.39E-05 4.37E-04 9.04E-02 0.5

Cadmium (Cd) 4.25E-02 2.88E-05 4.25E-02 0.07 4.75E-02 9.35E-06 4.76E-02 2.41E-02 3.79E-05 2.42E-02 1.14E-01 7.61E-05 1.14E-01 0.07 2.36E-04 1.71E-05 5.17E-05 3.05E-04 1.15E-01 0.3

Hydrogen chloride (HCl) 3.44E+01 2.90E-04 3.44E+01 0.001 3.90E+01 0.00E+00 3.90E+01 4.80E+02 8.35E-03 4.80E+02 5.53E+02 8.64E-03 5.53E+02 0.002 5.53E+02

Chromium (Cr) 3.28E-01 2.86E-05 3.28E-01 0.009 3.66E-01 9.35E-06 3.66E-01 1.78E-01 3.77E-05 1.78E-01 8.72E-01 7.56E-05 8.72E-01 0.009 4.03E-03 3.12E-04 1.18E-03 5.52E-03 8.77E-01 0.6

Cobalt (Co) 7.19E-02 8.51E-05 7.20E-02 0.1 8.01E-02 2.84E-05 8.01E-02 4.05E-02 1.13E-04 4.06E-02 1.92E-01 2.26E-04 1.93E-01 0.1 2.71E-03 2.94E-05 7.68E-04 3.50E-03 1.96E-01 1.8

Hydrogen fluoride (HF) 9.48E+00 0.00E+00 9.48E+00 0.0 1.08E+01 0.00E+00 1.08E+01 9.33E+01 0.00E+00 9.33E+01 1.14E+02 0.00E+00 1.14E+02 0.0 1.14E+02

Lead (Pb) 4.64E-01 8.71E-05 4.64E-01 0.02 5.14E-01 2.80E-05 5.14E-01 1.83E-01 1.14E-04 1.83E-01 1.16E+00 2.29E-04 1.16E+00 0.02 3.86E-03 9.41E-05 7.21E-04 4.68E-03 1.17E+00 0.4

Manganese (Mn) 5.06E-01 6.20E-05 5.06E-01 0.01 5.65E-01 1.87E-05 5.65E-01 3.24E-01 7.92E-05 3.24E-01 1.40E+00 1.60E-04 1.40E+00 0.01 9.16E-03 4.70E-03 3.69E-03 1.75E-02 1.41E+00 1.2

Mercury (Hg) 6.39E-02 2.80E-05 6.40E-02 0.04 7.25E-02 9.35E-06 7.25E-02 1.07E-01 3.72E-05 1.07E-01 2.44E-01 7.46E-05 2.44E-01 0.03 2.88E-05 5.00E-07 4.03E-06 3.33E-05 2.44E-01 0.0

Nickel (Ni) 3.31E-01 2.90E-05 3.31E-01 0.009 3.71E-01 9.35E-06 3.71E-01 1.77E-01 3.82E-05 1.78E-01 8.79E-01 7.65E-05 8.79E-01 0.009 3.85E-03 2.00E-04 1.07E-03 5.13E-03 8.84E-01 0.6

Selenium (Se) 3.31E-01 1.40E-04 3.31E-01 0.04 3.76E-01 4.67E-05 3.76E-01 6.41E-01 1.86E-04 6.41E-01 1.35E+00 3.73E-04 1.35E+00 0.03 5.04E-04 7.64E-05 1.24E-04 7.05E-04 1.35E+00 0.1

Organic HAP (CAS Number)

1,1-Dichloroethane (75343) 1.91E-02 1.91E-02 0.0 2.17E-02 2.17E-02 2.19E-02 2.19E-02 6.26E-02 6.26E-02 0.0 0.00E+00 6.26E-02

1,2-Dibromoethane (106934) 5.57E-02 5.57E-02 0.0 6.34E-02 6.34E-02 6.39E-02 6.39E-02 1.83E-01 1.83E-01 0.0 0.00E+00 1.83E-01

1,2-Dichloroethane (107062) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

1,2-Dichloropropane (78875) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

1,2,4-Trichlorobenzene (120821) 3.21E-02 3.21E-02 0.0 3.66E-02 3.66E-02 3.69E-02 3.69E-02 1.06E-01 1.06E-01 0.0 0.00E+00 1.06E-01

1,3-Dichloropropene (542756) 1.54E-02 1.54E-02 0.0 1.76E-02 1.76E-02 1.77E-02 1.77E-02 5.07E-02 5.07E-02 0.0 0.00E+00 5.07E-02

1,4-Dichlorobenzene (106467) 2.36E-02 2.36E-02 0.0 2.68E-02 2.68E-02 2.70E-02 2.70E-02 7.74E-02 7.74E-02 0.0 0.00E+00 7.74E-02

2-Butanone (78933) 6.64E-02 0.00E+00 6.64E-02 0.0 7.56E-02 0.00E+00 7.56E-02 7.62E-02 0.00E+00 7.62E-02 2.18E-01 0.00E+00 2.18E-01 0.0 0.00E+00 2.18E-01

2,4-Dinitrophenol (51285) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

2,4-Dinitrotoluene (121142) 4.28E-03 4.28E-03 0.0 4.88E-03 4.88E-03 4.92E-03 4.92E-03 1.41E-02 1.41E-02 0.0 0.00E+00 1.41E-02

2,4,6-Trichlorophenol (88062) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

3-Chloropropylene (107051) 1.95E-01 1.95E-01 0.0 2.22E-01 2.22E-01 2.24E-01 2.24E-01 6.40E-01 6.40E-01 0.0 0.00E+00 6.40E-01

4-Methyl-2-pentanone (108101) 4.93E-02 4.93E-02 0.0 5.61E-02 5.61E-02 5.65E-02 5.65E-02 1.62E-01 1.62E-01 0.0 0.00E+00 1.62E-01

4-Methylphenol (106445) 2.36E-02 2.36E-02 0.0 2.68E-02 2.68E-02 2.70E-02 2.70E-02 7.74E-02 7.74E-02 0.0 0.00E+00 7.74E-02

4-Nitrophenol (100027) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

Acetaldehyde (75070) 6.85E-02 0.00E+00 6.85E-02 0.0 7.80E-02 0.00E+00 7.80E-02 7.86E-02 0.00E+00 7.86E-02 2.25E-01 0.00E+00 2.25E-01 0.0 0.00E+00 2.25E-01

Acetophenone (98862) 2.57E-02 0.00E+00 2.57E-02 0.0 2.93E-02 0.00E+00 2.93E-02 2.95E-02 0.00E+00 2.95E-02 8.45E-02 0.00E+00 8.45E-02 0.0 0.00E+00 8.45E-02

Acrolein (107028) 4.07E-02 0.00E+00 4.07E-02 0.0 4.63E-02 0.00E+00 4.63E-02 4.67E-02 0.00E+00 4.67E-02 1.34E-01 0.00E+00 1.34E-01 0.0 0.00E+00 1.34E-01

Benzene (71432) 8.35E-02 0.00E+00 8.35E-02 0.0 9.51E-02 0.00E+00 9.51E-02 9.59E-02 0.00E+00 9.59E-02 2.74E-01 0.00E+00 2.74E-01 0.0 0.00E+00 2.74E-01

Benzyl chloride (100447) 6.00E-03 6.00E-03 0.0 6.83E-03 6.83E-03 6.88E-03 6.88E-03 1.97E-02 1.97E-02 0.0 0.00E+00 1.97E-02

Biphenyl (92524) 3.43E-03 3.43E-03 0.0 3.90E-03 3.90E-03 3.93E-03 3.93E-03 1.13E-02 1.13E-02 0.0 0.00E+00 1.13E-02

bis(2-Ethylhexyl)phthalate (117817) 7.71E-02 0.00E+00 7.71E-02 0.0 8.78E-02 0.00E+00 8.78E-02 8.85E-02 0.00E+00 8.85E-02 2.53E-01 0.00E+00 2.53E-01 0.0 1.72E-04 1.72E-04 2.54E-01 0.1

Bromomethane (74839) 1.91E-02 0.00E+00 1.91E-02 0.0 2.17E-02 0.00E+00 2.17E-02 2.19E-02 0.00E+00 2.19E-02 6.26E-02 0.00E+00 6.26E-02 0.0 0.00E+00 6.26E-02

Carbon disulfide (75150) 2.36E-02 2.36E-02 0.0 2.68E-02 2.68E-02 2.70E-02 2.70E-02 7.74E-02 7.74E-02 0.0 0.00E+00 7.74E-02

Carbon tetrachloride (56235) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

Chlorobenzene (108907) 3.43E-03 0.00E+00 3.43E-03 0.0 3.90E-03 0.00E+00 3.90E-03 3.93E-03 0.00E+00 3.93E-03 1.13E-02 0.00E+00 1.13E-02 0.0 0.00E+00 1.13E-02

Chloroethane (75003) 1.13E-02 1.13E-02 0.0 1.29E-02 1.29E-02 1.30E-02 1.30E-02 3.73E-02 3.73E-02 0.0 0.00E+00 3.73E-02

Chloroform (67663) 1.71E-02 0.00E+00 1.71E-02 0.0 1.95E-02 0.00E+00 1.95E-02 1.97E-02 0.00E+00 1.97E-02 5.63E-02 0.00E+00 5.63E-02 0.0 0.00E+00 5.63E-02

Chloromethane (74873) 2.36E-02 0.00E+00 2.36E-02 0.0 2.68E-02 0.00E+00 2.68E-02 2.70E-02 0.00E+00 2.70E-02 7.74E-02 0.00E+00 7.74E-02 0.0 0.00E+00 7.74E-02

Dibenzofuran (132649) 1.24E-02 1.24E-02 0.0 1.41E-02 1.41E-02 1.43E-02 1.43E-02 4.08E-02 4.08E-02 0.0 0.00E+00 4.08E-02

Dibutylphthalate (84742) 2.36E-03 2.36E-03 0.0 2.68E-03 2.68E-03 2.70E-03 2.70E-03 7.74E-03 7.74E-03 0.0 0.00E+00 7.74E-03

Dimethylphthalate (131113) 1.93E-03 1.93E-03 0.0 2.19E-03 2.19E-03 2.21E-03 2.21E-03 6.33E-03 6.33E-03 0.0 0.00E+00 6.33E-03

Ethyl benzene (100414) 1.71E-02 0.00E+00 1.71E-02 0.0 1.95E-02 0.00E+00 1.95E-02 1.97E-02 0.00E+00 1.97E-02 5.63E-02 0.00E+00 5.63E-02 0.0 0.00E+00 5.63E-02

Formaldehyde (50000) 5.57E-02 4.12E-03 5.98E-02 6.9 6.34E-02 1.37E-03 6.48E-02 6.39E-02 5.46E-03 6.94E-02 1.83E-01 1.09E-02 1.94E-01 5.6 0.00E+00 1.94E-01

n-Hexane (110543) 1.05E-02 1.05E-02 0.0 1.20E-02 1.20E-02 1.20E-02 1.20E-02 3.45E-02 3.45E-02 0.0 0.00E+00 3.45E-02

Hexachlorobenzene (118741) 8.78E-05 8.78E-05 0.0 1.00E-04 1.00E-04 1.01E-04 1.01E-04 2.89E-04 2.89E-04 0.0 0.00E+00 2.89E-04

Iodomethane (74884) 4.28E-02 4.28E-02 0.0 4.88E-02 4.88E-02 4.92E-02 4.92E-02 1.41E-01 1.41E-01 0.0 0.00E+00 1.41E-01

Isophorone (78591) 2.57E-02 2.57E-02 0.0 2.93E-02 2.93E-02 2.95E-02 2.95E-02 8.45E-02 8.45E-02 0.0 0.00E+00 8.45E-02

Methyl chloroform (71556) 1.31E-02 0.00E+00 1.31E-02 0.0 1.49E-02 0.00E+00 1.49E-02 1.50E-02 0.00E+00 1.50E-02 4.29E-02 0.00E+00 4.29E-02 0.0 0.00E+00 4.29E-02

Methyl methacrylate (80626) 2.36E-02 2.36E-02 0.0 2.68E-02 2.68E-02 2.70E-02 2.70E-02 7.74E-02 7.74E-02 0.0 0.00E+00 7.74E-02

Methylene chloride (75092) 7.71E-02 0.00E+00 7.71E-02 0.0 8.78E-02 0.00E+00 8.78E-02 8.85E-02 0.00E+00 8.85E-02 2.53E-01 0.00E+00 2.53E-01 0.0 0.00E+00 2.53E-01

Naphthalene (91203) 1.33E-02 0.00E+00 1.33E-02 0.0 1.51E-02 0.00E+00 1.51E-02 1.52E-02 0.00E+00 1.52E-02 4.36E-02 0.00E+00 4.36E-02 0.0 4.13E-04 1.71E-07 4.13E-04 4.40E-02 0.9

Pentachlorophenol (87865) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

Phenol (108952) 7.07E-02 0.00E+00 7.07E-02 0.0 8.05E-02 0.00E+00 8.05E-02 8.11E-02 0.00E+00 8.11E-02 2.32E-01 0.00E+00 2.32E-01 0.0 3.10E-03 3.10E-03 2.35E-01 1.3

Polychlorinated biphenyl [PCB] (1336363) 3.21E-04 0.00E+00 3.21E-04 0.0 3.66E-04 0.00E+00 3.66E-04 3.69E-04 0.00E+00 3.69E-04 1.06E-03 0.00E+00 1.06E-03 0.00 0.00E+00 1.06E-03

Propionaldehyde (123386) 4.07E-02 0.00E+00 4.07E-02 0.0 4.63E-02 0.00E+00 4.63E-02 4.67E-02 0.00E+00 4.67E-02 1.34E-01 0.00E+00 1.34E-01 0.00 0.00E+00 1.34E-01

Styrene (100425) 1.50E-02 0.00E+00 1.50E-02 0.0 1.71E-02 0.00E+00 1.71E-02 1.72E-02 0.00E+00 1.72E-02 4.93E-02 0.00E+00 4.93E-02 0.00 0.00E+00 4.93E-02

Tetrachloroethylene (127184) 8.99E-03 0.00E+00 8.99E-03 0.0 1.02E-02 0.00E+00 1.02E-02 1.03E-02 0.00E+00 1.03E-02 2.96E-02 0.00E+00 2.96E-02 0.00 0.00E+00 2.96E-02

Toluene (108883) 3.64E-02 0.00E+00 3.64E-02 0.0 4.15E-02 0.00E+00 4.15E-02 4.18E-02 0.00E+00 4.18E-02 1.20E-01 0.00E+00 1.20E-01 0.00 0.00E+00 1.20E-01

Trichloroethylene (79016) 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00 N/A 0.00E+00 0.00E+00

Vinyl acetate (108054) 6.64E-03 6.64E-03 0.0 7.56E-03 7.56E-03 7.62E-03 7.62E-03 2.18E-02 2.18E-02 0.0 0.00E+00 2.18E-02

Vinyl chloride (75014) 1.56E-02 0.00E+00 1.56E-02 0.0 1.78E-02 0.00E+00 1.78E-02 1.79E-02 0.00E+00 1.79E-02 5.14E-02 0.00E+00 5.14E-02 0.0 0.00E+00 5.14E-02

Xylenes (1330207) 2.70E-02 0.00E+00 2.70E-02 0.0 3.07E-02 3.07E-02 3.10E-02 3.10E-02 8.87E-02 8.87E-02 0.0 0.00E+00 8.87E-02

Polycyclic organic matter (POM) 2.84E-02 2.23E-04 2.86E-02 0.8 3.23E-02 7.42E-05 3.24E-02 3.26E-02 2.95E-04 3.29E-02 9.32E-02 5.92E-04 9.38E-02 0.6 4.41E-03 6.64E-07 4.41E-03 9.82E-02 4.5

2,3,7,8-Tetrachlorodibenzo-p-dioxin (1746-01-6) 8.35E-09 0.00E+00 8.35E-09 0.0 9.51E-09 0.00E+00 9.51E-09 9.59E-09 0.00E+00 9.59E-09 2.74E-08 0.00E+00 2.74E-08 0.0 0.00E+00 2.74E-08

Organic HAP Total 1.43E+00 4.34E-03 1.44E+00 0.3 1.63E+00 1.45E-03 1.63E+00 1.64E+00 5.75E-03 1.65E+00 4.71E+00 1.15E-02 4.72E+00 0.2 8.09E-03 8.35E-07 8.09E-03 4.73E+00 0.2

Ci/yr % Ci/yr Ci/yr Ci/yr % Ci/yr %

Radionuclides 7.35E-02 7.35E-02 0.0 8.11E-02 8.11E-02 4.17E-02 4.17E-02 1.96E-01 1.96E-01 7.03E-04 7.03E-04 1.97E-01 0.4

Notes:

(1) CY05 PAF coal-region proximate coal-quality data from Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. Unit-specific total coal-burn quantities listed in Excel file "CY05 Operating

 Statistics from DataFuser (012306).xls" on FPG Env Affr - TRI server were apportioned according to coal-region breakdown listed in Excel file "CoalStats2005.xls" in 1-19-06 e-mail fr. M.A. Pendley to J.D. Lokey (for PAF Units 1-2)

 or in previously cited Excel file in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al. (PAF Unit 3); CEMS data from Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey;

 ash split to bottom ash from Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(2) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06). Concentrations were

 weighted for each PAF coal-supply region by CY05 dry-basis tonnage burned in the plant/subplant. LT Model data were derived from EPRI's PISCES Database, except mercury (Hg) and chlorine (Cl)

 were taken from EPA's Information Collection Request (ICR) Part II coal database, May 2000. Coal-fired trace-element emission estimates in this file are based on LT Model coal concentrations, except

 for hydrogen chloride (HCl) estimates, which are based on Cl data from TVA's CY99 ICR analyses (per 3-16-00 e-mail from J.D. Eady to R.W. Burbage). Concentrations of semivolatile organic compounds

 in coal (unspecified coal region) were taken from PISCES database as listed in 2-13-01 e-mail from P. Chu (EPRI) to I.J. Berty (SAIC) et al.

(3) Trace-element, organic HAP & radionuclide emissions were estimated using median emission factors from EPRI's "Emission Factors Handbook[EFH]--Guidelines for Estimating Trace Substance Emissions

 from Fossil Fuel Steam Electric Plants", Report No. EPRI TR-105611, Nov. 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update. For certain organic pollutants listed as

 nondetects in the EFH, emission factors were derived from EPRI's PISCES database using EFH procedures (per e-mails from J.D. Lokey to T.A Burnett [2-13-01] & to P. Chu [2-23-01]). Criteria-pollutant

 emissions were estimated from stack tests (filterable PM), continuous emission monitoring system (CEMS) data (SO2 & NOx), and AP-42 emission factors (condensable PM, CO & VOC) or particle-size

 distributions (PM10_fil & PM2.5_fil). Ash-handling fugitive-dust emissions of semivolatile organic compounds (e.g., POM) were estimated based on reported fly-ash and bottom-ash concentrations

 (5-29-01 e-mail from N. Goodman (EPRI) to J.D. Lokey).

(4) CY01-CY05 filterable-PM stack test results from Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at US DOE-FETC Conference on Formation, Distribution,

 Impact, and Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid

 Emissions from Coal-Fired Power Plants"); by L.S. Monroe, 5-01; by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from

 Stationary Power Plants"); and by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(6) Ammonia RY2005 Release Calculator model (v0.3), from S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05, TVA Environmental Technologies 

 using CY05 selective-catalytic-reduction (SCR) process operational data & vendor-guaranteed SCR-exit max NH3 slip (2 ppmv dry basis) at 20,000 SCR operating hours. 07/12/06

Page 1 of 1
BART

TVA Paradise Fossil Plant (PAF) BART Modeling Protocol Emission Estimates

latitude longitude Datum UTM East UTM North UTM Zone Datum

deg. deg. km km ft ft ft ft/s deg F lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr

PAF1 TVA - PAF Unit 1 37.261 86.979 501.91 4123.61 16 600 422 26.0 72.6 125 4,371 321 3,695 686 527 2.39E-04

PAF2 TVA - PAF Unit 2 37.260 86.979 501.87 4123.56 16 600 422 26.0 72.6 125 4,528 321 3,692 676 522 2.49E-04

PAF3 TVA - PAF Unit 3 37.260 86.980 501.78 4123.48 16 800 422 26.79 134 327 26,477 372 5,090 852 723 3.04

Stack ID # Company/Source

Location Location UTM Stack 

Height

Base 

Elevation Diameter NOx 

Emissions

PM10 

Emissions

PM2.5 

Emissions

NH3 

Emissions

Gas Exit 

Velocity

Stack Gas 

Exit Temp.

SO2 

Emissions

H2SO4 

Emissions

Page 1 of 2
BART

PAF1

PAF2

PAF3

Stack ID #

Condensable Particulate Matter (CPM) Filterable Particulate Matter < 10-micrometer (μm) aerodynamic diameter (PM10_fil)

particle speciation Organic CPM (CPM-ORG)

Inorganic CPM (CPM-IOR), 

taken to be H2SO4 Coarse PM Soil Elemental Carbon (EC)

filterable 

PM10

condensable 

PM10 0.625-1.0 μm < 0.625 μm 0.625-1.0 μm < 0.625 μm 6-10 μm 2.5-6 μm 1.25-2.5 μm 1.0-1.25 μm 0.625-1.0 μm < 0.625 μm 1.25-2.5 μm 1.0-1.25 μm 0.625-1.0 μm < 0.625 μm

% % lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr lbs/hr

49 51 13.9 13.9 161 161 59.5 99.1 69.4 24.8 77.7 0.0 0.0 0.0 0.0 6.60

48 52 13.9 13.9 161 161 57.6 96.1 67.3 24.0 75.3 0.0 0.0 0.0 0.0 6.40

32 68 103 103 186 186 48.4 80.7 56.5 20.2 63.2 0.0 0.0 0.0 0.0 5.37

0.625-1.0 μm < 0.625 μm 0.625-1.0 μm < 0.625 μm 6-10 μm 2.5-6 μm 1.25-2.5 μm 1.0-1.25 μm 0.625-1.0 μm < 0.625 μm 1.25-2.5 μm 1.0-1.25 μm 0.625-1.0 μm < 0.625 μm

50 50 50 50 17.6 29.4 20.6 7.4 23.0 0.0 0.0 0.0 0.0 2.0

*Reference: "Particulate Speciation Profiles for Selected Source Types" posted 3-16-06 on VISTAS website providing CALPUFF

modeling information for BART applications (http://vistas-sesarm.org/BART/calpuff.asp); PM speciation files from this website

correspond with Excel files (e.g., "2006FinalCycloneFurnaceESPpmSpeciationProfile.xls") downloaded from National Park Service

(NPS) website (http://www2.nature.nps.gov/air/permits/ect/ectCoalFiredBoiler.cfm)

TVA Environmental Technologies

07/12/06

Assumed CPM-ORG Assumed CPM-IOR Fraction (%) of Filterable PM10 (PM10_fil) in each class/size range*

Particle-Size Distributn, % Particle-Size Distributn, % Coarse Soil Elemental Carbon (EC)

Page 2 of 2
Inputs

Table 7. Gaseous-Species Emission Parameters & Molecular Wts Table 8. EPRI EFH Recommended Emission Factor*

Boiler Coal Boiler SO3 Production, Median Gas-phase Fraction at Stack* (as % of Coal Input)

Type Type SO3/SO2 Molar Ratio Nitrogen Oxides (NOx), Sulfur Oxides (SOx) as SO2, Without FGD With FGD Molecular Coal Type/Contrl Sys Pollutant Control

Dry-bottom Low-S Eastern Bituminous (LSE) 0.008 Coal Type lb/(ton as-fired coal) lb/(ton as-fired coal*%S) Pollutant Scrubbers Scrubbers Weight** (Se, HCl, HF) Se HCl HF Hg Device (Hg)

Pulverized- High-S Eastern Bituminous (HSE) 0.011 Bituminous 33 38 Chloride (Cl) 0.993 0.953 35.453 Bituminous/non-FGD 55 100 90 ** non-FGD

Coal (PC) Western Bituminous 0.00111 Subbituminous 17 35 Fluoride (F) 0.986 0.920 18.9984 Lignite/non-FGD 55 100 90 ** FGD

Subbituminous (PRB) 0.0014 Hydrogen chloride (HCl) 36.4609 Subbituminous 3 20 50

Lignite 0.0048 *Reference: US EPA, Compilation of Air Pollutant Emission Factors (AP-42), Hydrogen fluoride (HF) 20.0063 Bitum or Lignite/FGD 12 3 6

Cyclone Eastern Bituminous 0.016 Vol. I, 5th Edition, Supplement E, Section 1.1, "Bituminous and Subbituminous Mercury (Hg) 200.59

Western Bituminous 0.0022 Coal Combustion", Table 1.1-3, Sept. 98. Selenium (Se) 78.96 *Reference: Emission Factors Handbook (EFH) Guidelines for Estimating Trace

Subbituminous (PRB) 0.003 Sulfur (S) 32.064 Substance Emissions from Fossil Fuel Steam Electric Plants, Electric Power

Lignite 0.00112 Table 6. Particulate-Matter (PM) Particle-Size Distribution for Sulfur Dioxide (SO2) 64.0628 Research Institute (EPRI), EPRI TR-105611, 11-95, as updated in 9-98 & 2-01

Cyclone-Fired Boilers Burning Bituminous Coal* Sulfur Trioxide (SO3) 80.0622 EFH Addenda and in the Apr. 2002 EFH revision.

Table 2. Air-Heater (AH) SO3/H2SO4 Penetration (F2) Factors* Sulfuric Acid (H2SO4) 98.0774

Boiler Coal SO3/H2SO4 Penetration Particle Size Ammonia 17.0304 **Apr. 02 EFH Revision predicts Hg removal using correlation equations developed

Type Type Factr ( = 1 - contrl efficncy) (Aerodynamic Nitrogen Oxides (NOx) as Nitrogen Dioxide (NO2) 46.0055 from 1999 ICR stack-test program results. Hg removal varies with chloride content

All Low-S Eastern Bituminous (LSE) 0.49 Equiv. Diameter), Electrostatic of coal. Different correlation equations are listed for various types of air-pollution

High-S Eastern Bituminous (HSE) 0.85 Micrometers Uncontrolled Precipitator (ESP) *Reference: PISCES Version 2.1 Release Notes, Addendum 3-6-98 control equipment.

Western & Subbituminous (PRB) 0.90 10 13 68

6 8 56 **Reference: Chemical Engineers' Handbook, 5th Edition, Note: FGD = flue-gas desulfurization, e.g., limestone scrubber.

Table 3. PM-Control Eqpmt SO3/H2SO4 Penetratn (F2) Factrs* 2.5 5.5 36 R.H. Perry & C.H. Chilton, Editors, 1973

Eqpmt Coal SO3/H2SO4 Penetration 1.25 5 22

Type Type Factr ( = 1 - contrl efficncy) 1 5 17

Cold-side Low-S Eastern Bituminous (LSE) 0.49 0.625 0

ESP High-S Eastern Bituminous (HSE) 0.77

Western & Subbituminous (PRB) 0.50 *Reference: US EPA, Compilation of Air Pollutant Emission Factors (AP-42),

Hot ESP All 0.63 Vol. I, 5th Edition, Supplement E, Section 1.1, Table 1.1-8, Sept. 98.

Bagfilter (BF) All 0.10

No data were given in Table 1.1-8 for particle-size distributions for cyclone coal-fired

Table 4. Wet/Dry FGD Eqpmt SO3/H2SO4 Penetratn (F2) Factrs* boilers controlled by flue-gas-desulfurization (FGD) scrubbers, nor in size range below

Eqpmt Coal SO3/H2SO4 Penetration 0.625 microns for any controls. PM-10 and PM-2.5 emssns for PAF Units 1-2 were

Type Type Factr ( = 1 - contrl efficncy) estimated using the particle-size distribution for cyclone boilers controlled by ESP.

Wet Spray Eastern Bituminous 0.47

Tower PRB/Lignite 0.40 Table 6A. Fine Filterable PM (PM2.5_fil) Chemical Speciation* 

Wet Venturi All 0.65

Dry FGD/BF All 0.01 Elemental Carbon (EC), Soil (e.g., flyash),

Mg-Ox mixed All 0.50 Equipment Type % of PM2.5_fil % of PM2.5_fil

with fuel oil Coal-fired Boilers 3.7 96.3

Mg-Ox into All 0.50

furnace *Reference: US EPA, Draft "Catalog of Global Emissions Inventories and Emission 

Inventory Tools for Black Carbon", Jan. 2002, as cited in "Particulate Speciation Profiles

Nominal Stack Flue-gas O2 Concentratn, % Vol = 6.0 for Selected Source Types" posted 3-16-06 on website providing CALPUFF modeling

Nominal Flue-gas H2O Concentratn, % Vol = 8.1 information for VISTAS BART applications (http://vistas-sesarm.org/BART/calpuff.asp)

NOTE: O2 concen. is used to estimate approx. SO3 volumetric concentration for Table 6B. Total Condensable PM (CPM-TOT) Emission Factors* 

comparison purposes. The SO3/H2SO4 mass emission rate (tpy) is estimated

based on SO3/SO2 molar ratio, so precise O2 concen. aren't needed (changing Emission Factor (lb/10^6 Btu) vs. coal sulfur (S) content (%)

the O2 concen. doesn't change the H2S04 mass emission rate, only ppm SO3). Equipment Type Coal S <= 0.4% by weight Coal S > 0.4% by weight

PC Blr w/o FGD 0.01 =0.1*S-0.03

*Reference: "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power PC Blr w/ FGD 0.02 0.02

 Plants", by R. Hardman, R. Stacy, & E. Dismukes. Paper presented at U.S. Cyclone Blr w/o FGD 0.01 =0.1*S-0.03

 DOE-FETC Conference on Formation, Distribution, Impact, and Fate of Sulfur Cyclone Blr w/ FGD 0.02 0.02

 Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, 3-98; revised by K. Harrison, AFBC Blr 0.02 0.02

 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric

 Acid Emissions from Coal-Fired Power Plants"); and by L.S. Monroe, 5-01, by Table 6C. Condensable Particulate Matter (CPM) Chemical Speciation* 

 L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for

 Estimating Total Sulfuric Acid Emissions from Stationary Power Plants"), and Inorganic CPM (CPM-IOR), Organic CPM (CPM-ORG),

 by K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Equipment Type % of CPM-TOT % of CPM-TOT

 Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)"). PC Blr w/o FGD 80 20

PC Blr w/ FGD ND, assume same as above ND, assume same as above

Note: High-sulfur E. bituminous coal is defined as >= 2.5 % S, per 2-17-06 e-mail Cyclone Blr w/o FGD 80 20

from K.E. Harrison to J.D. Lokey et al. Cyclone Blr w/ FGD ND, assume same as above ND, assume same as above

*Reference: US EPA, Compilation of Air Pollutant Emission Factors (AP-42), TVA Environmental Technologies

Vol. I, 5th Edition, Supplement E, Section 1.1, Table 1.1-5, Sept. 98. 07/12/06

PM Cumulative Size Distribution,

Cumulative Mass % < Stated Size

Table 1. Coal-fired Boiler SO3/H2SO4 Production (F1) Factors* Table 5. Uncontrolled Cyclone-Furnace Emission Factors*

Page 1 of 1
Outputs

Estimated Elemental Concentrations in PAF Solids Streams, mg/kg

PAF 1-2 PAF 1-3 PAF 1-3 PAF 1-3 PAF 1-2

Species Coal (dry) Coal (dry)

Bottom 

Ash + Pyr

Fly Ash to 

Ash Pond Gypsum

Sb 2.40 4.13 3.43 219 14.5

As 11.08 8.87 8.9 206 67.9

Ba 75.9 103.4 798 716 294

Be 1.66 1.37 3.09 28.2 8.8

Cd 1.05 0.92 2.67 19.0 5.17

Cl 625 494 67.0 686 4017

Cr 18.8 15.6 92 189 60.0

Co 13.0 10.5 57.7 124 43.0

Cu 12.2 11.5 39.2 262 56.8

F 8.78 15.9 38.5 373 82.1

Pb 18.7 15.0 17.9 336 108

Mn 40.1 35.5 342 128 84.4

Hg 0.113 0.111 0.316 0.30 0.201

Mo 12.0 10.2 42.5 170 54.5

Ni 16.8 14.9 81 220 59.2

Se 2.38 1.95 7.9 18.5 9.6

Ag 0.12 0.186 1.48 1.70 0.315

Tl 2.13 2.32 6.08 63.9 11.6

V 70.9 58.0 383 585 184

Zn 54.1 43.8 109 899 274

Note:

PAF 1-2 Fly_Ash_Capture to gypsum stack = 90% Remainder goes to slag pond (economizer ash)

PAF Unit 3 Fly_Ash_Capture to ash pond = 100%

*Reference: PISCES Model (ver. 3.11) outputs, obtained from 3-11-02 P31 file on "envshr" drive .

Page 1
calcs

Sample Calculations for CY05 Paradise Fossil Plant (PAF) Unit 1 Coal-fired Criteria-Pollutant & Hazardous-Air-Pollutant (HAP) Emission Estimates 

General Input Variables: Value Units Notes Reference

coal_burn_PAF1_2 = 3,994,078 tons/yr (tpy) CY05 PAF Units 1-2 as received/fired (AR) coal burn (total for all coal-supply regions) 1

coal_burn_PAF3 = 2,569,468 tpy CY05 PAF Unit 3 AR coal burn (total for all coal-supply regions) 1

coal_burn_PAF1_2_ILB = 3,946,354 tpy CY05 PAF Units 1-2 AR Illinois Basin (ILB) bituminous coal burn 1

coal_burn_PAF1_2_PRB = 47,724 tpy CY05 PAF Units 1-2 AR Powder River Basin (PRB) subbituminous coal burn 1

coal_burn_PAF3_ILB = 745,146 tpy CY05 PAF Unit 3 AR ILB bituminous coal burn 1

coal_burn_PAF3_PRB = 1,824,322 tpy CY05 PAF Unit 3 AR PRB subbituminous coal burn 1

coal_burn_PAF1 = 1,866,460 tpy CY05 PAF Unit 1 AR coal burn (total for all coal-supply regions) 2

coal_burn_PAF2 = 2,127,618 tpy CY05 PAF Unit 2 AR coal burn (total for all coal-supply regions) 2

coal_burn_PAF3 = 2,569,468 tpy CY05 PAF Unit 3 AR coal burn (total for all coal-supply regions) 2

coal_burn_PAF1_ILB_coal_stats = 1,847,875 tpy CY05 PAF Unit 1 AR ILB bituminous coal burn (from PAF coal statistics) 3

coal_burn_PAF1_PRB_coal_stats = 18,585 tpy CY05 PAF Unit 1 AR PRB subbituminous coal burn (from PAF coal statistics) 3

coal_burn_PAF2_ILB_coal_stats = 2,091,644 tpy CY05 PAF Unit 2 AR ILB bituminous coal burn (from PAF coal statistics) 3

coal_burn_PAF2_PRB_coal_stats = 29,139 tpy CY05 PAF Unit 2 AR PRB subbituminous coal burn (from PAF coal statistics) 3

coal_H2O_PAF_ILB = 12.2 %-weight CY05 PAF ILB coal H2O content 1

coal_H2O_PAF_PRB = 27.5 %-weight CY05 PAF PRB coal H2O content 1

coal_ash_PAF_ILB = 8.6 %-weight CY05 PAF ILB coal AR ash content 1

coal_ash_PAF_PRB = 5.3 %-weight CY05 PAF PRB coal AR ash content 1

coal_S_PAF_ILB = 2.69 %-weight CY05 PAF ILB coal AR sulfur content 1

coal_S_PAF_PRB = 0.35 %-weight CY05 PAF PRB coal AR sulfur content 1

coal_heat_PAF_ILB = 11,500 Btu [HHV]/lb CY05 PAF ILB coal AR heat content (higher heating value [HHV]) 1

coal_heat_PAF_PRB = 8,775 Btu [HHV]/lb CY05 PAF PRB coal AR heat content (HHV) 1

PM_fil_emssn_factr_PAF1_coal = 0.071 lb/10^6 Btu (MBtu) Average of CY01-CY05 PAF Unit 1 coal-fired filterable particulate-matter (PM_fil) stack-test measurements 4

ash_partition_to_flue_gas_PAF = 25 % TVA data for ash distribution in PAF cyclone-furnace coal-fired boilers 5

PM_fil_sub10_ESP = 68 % Cumulative PM_fil mass % <= 10 micrometers for bituminous-fired cyclone blrs w/ electrostatic precipitator (ESP) 6

PM_fil_sub6_ESP = 56 % Cumulative PM_fil mass % <= 6 micrometers for bituminous-fired cyclone blrs w/ ESP 6

PM_fil_sub2.5_ESP = 36 % Cumulative PM_fil mass % <= 2.5 micrometers for bituminous-fired cyclone blrs w/ ESP 6

PM_fil_sub1.25_ESP = 22 % Cumulative PM_fil mass % <= 1.25 micrometers for bituminous-fired cyclone blrs w/ ESP 6

PM_fil_sub1_ESP = 17 % Cumulative PM_fil mass % <= 1.0 micrometers for bituminous-fired cyclone blrs w/ ESP 6

PM_cond_emssn_factr_coal_FGD = 0.02 lb/MBtu Condensable particulate-matter (PM_cond) emssn factr for cyclone blrs w/ flue-gas-desulfurization (FGD) scrubber 6

PM_cond_org_fractn = 20 % Organic fraction (%) of total PM_cond emissns for cyclone blrs (use same factr as for pulverized-coal [PC] blrs) 6

CO_uncontrlld_emssn_factr_coal = 0.5 lb/(ton AR coal) Uncontrolled carbon monoxide (CO) emssn factr for cyclone-fired blrs 6

VOC_uncontrlld_emssn_factr_coal = 0.11 lb/(ton AR coal) Uncontrolled volatile organic compound (VOC) emssn factr for cyclone-fired blrs 6

SO2_emssn_PAF1_CEMS = 13,563 tpy CY05 PAF Unit 1 CEMS sulfur dioxide (SO2) emssn data (coal + alternate fuels) 7

NOx_emssn_PAF1_CEMS = 11,466 tpy CY05 PAF Unit 1 CEMS nitrogen oxides (NOx) emssn data (coal + alternate fuels) 7

heat_input_PAF1_CEMS = 43,191,735 x 10^6 Btu/yr (MBtu/yr) CY05 PAF Unit 1 CEMS heat-input estimate (coal + alternate fuels) 7

max_heat_input_PAF1 = 6,959 x 10^6 Btu/hr (MBtu/hr) PAF Unit 1 maximum rated heat-input capacity, per Title V permit application 32

PM2.5_fil_EC_fractn = 3.7 % Elemental-carbon (EC) fraction (%) of PM_fil < 2.5 micrometers for coal-fired blrs 34

PM & Gaseous Trace-Element HAP Inputs:

Pb_in_ILB_mass = 14 mg/kg (dry basis) Median lead (Pb) concentration in Illinois Basin (ILB) bitum. coal 8

Pb_in_PRB_mass = 3.2 mg/kg (dry basis) Median Pb concentration in Powder River Basin (PRB) subbitum. coal 8

Cl_in_ILB_mass = 602 mg/kg (AR) CY99 Information Collection Request (ICR) AR chloride (Cl) concen. in PAF ILB coal receipts 9

Cl_in_PRB_mass = 50 mg/kg (AR) CY99 ICR AR Cl concentration in PAF PRB coal receipts 9

Hg_in_ILB_mass = 0.08 mg/kg (dry basis) Median mercury (Hg) concentration in ILB bitum. coal 8

Hg_in_PRB_mass = 0.06 mg/kg (dry basis) Median Hg concentration in PRB subbitum. coal 8

Cl_contrl_effncy_FGD = 97 % Emission Factor Hdbk (EFH) average Cl contrl effncy for coal-fired blrs w/ flue-gas-desulfurizatn (FGD) scrubber 10

Cl_mol_wt = 35.453 lb/lb-mole Chlorine atomic weight 11

HCl_mol_wt = 36.4609 lb/lb-mole Hydrogen chloride molecular weight 11

Hg_removal_multiplier_FGDW = 0.0582 dimensionless EFH Hg contrl-effncy equatn parameter for blrs w/ wet FGD scrubber but no electrostatic-precipitator (ESP) 10

Hg_removal_constant_FGDW = -0.1932 dimensionless EFH Hg contrl-effncy equatn parameter for blrs w/ wet FGD scrubber but no electrostatic-precipitator (ESP) 10

Hg_removal_effncy_SCR_FGDW_bitum = 86 % Hg removal efficiency for Eastern-bitum-fired boilers w/selective-catalytic-reduction (SCR) reactor & FGD scrubber 10

PAF Unit 1 Routine Coal-fired Criteria-Pollutant Emission Estimates:

Coal-fired total filterable particulate-matter (PM_fil) emissions were estimated from average of CY01-CY05 stack-test results. Filterable PM10 and PM2.5 emissions for PAF Units 1-3 were estimated based on AP-42 particle-size

distributions for cyclone-fired boilers with electrostatic-precipitator (ESP) PM control systems. No particle-size distribution data were listed for cyclone-fired boilers with flue-gas-desulfurization (FGD) scrubbers. Sulfur dioxide (SO2) 

and nitrogen oxides (NOx) emission estimates reflect continuous emission monitoring system (CEMS) data (coal-fired SO2 & NOx emissions were estimated by subtracting alternate-fuel estimates from CEMS data).

Condensable PM, carbon monoxide (CO), and volatile organic compound (VOC) emission estimates were derived from AP-42 emission factors.

Filterable Particulate Matter (PM_fil)

Equation (1):

coal_burn_PAF = coal_burn_PAF1_2+coal_burn_PAF3

coal_burn_PAF = 6,563,546 tons/yr (tpy)

Equation (2):

coal_burn_PAF1_ILB = coal_burn_PAF1*coal_burn_PAF1_ILB_coal_stats/(coal_burn_PAF1_ILB_coal_stats+coal_burn_PAF1_PRB_coal_stats)

coal_burn_PAF1_ILB = 1,847,875 tpy CY05 PAF Unit 1 Illinois Basin (ILB) bitum. coal AR coal-burn quantity (burn share based on PAF coal stats)

Equation (3):

coal_burn_PAF1_PRB = coal_burn_PAF1*coal_burn_PAF1_PRB_coal_stats/(coal_burn_PAF1_ILB_coal_stats+coal_burn_PAF1_PRB_coal_stats)

coal_burn_PAF1_PRB = 18,585 tpy CY05 PAF Unit 1 Powder River Basin (PRB) subbitum. coal AR coal-burn quantity (burn share based on PAF coal stats)

Equation (4):

coal_burn_PAF2_ILB = coal_burn_PAF2*coal_burn_PAF2_ILB_coal_stats/(coal_burn_PAF2_ILB_coal_stats+coal_burn_PAF2_PRB_coal_stats)

coal_burn_PAF2_ILB = 2,098,385 tpy CY05 PAF Unit 2 ILB bitum. coal AR coal-burn quantity (burn share based on PAF coal stats)

Equation (5):

coal_burn_PAF2_PRB = coal_burn_PAF2*coal_burn_PAF2_PRB_coal_stats/(coal_burn_PAF2_ILB_coal_stats+coal_burn_PAF2_PRB_coal_stats)

coal_burn_PAF2_PRB = 29,233 tpy CY05 PAF Unit 2 PRB subbitum. coal AR coal-burn quantity (burn share based on PAF coal stats)

Equation (6):

heat_input_PAF1_ILB = coal_burn_PAF1_ILB*(2000 lb/ton)*coal_heat_PAF_ILB*(TBtu/10^12 Btu)

heat_input_PAF1_ILB = 42.50 TBtu/yr

Equation (7):

heat_input_PAF1_PRB = coal_burn_PAF1_PRB*(2000 lb/ton)*coal_heat_PAF_PRB*(TBtu/10^12 Btu)

heat_input_PAF1_PRB = 0.33 TBtu/yr

Equation (8):

heat_input_PAF1_coal = heat_input_PAF1_ILB+heat_input_PAF1_PRB

heat_input_PAF1_coal = 42.83 TBtu/yr

Equation (9):

PM_fil_emssn_PAF1_coal = heat_input_PAF1_coal*(10^6 MBtu/TBtu)*PM_fil_emssn_factr_PAF1_coal*(ton/2000 lb)

PM_fil_emssn_PAF1_coal = 1.53E+03 tpy This value is listed in cell F21 of "PAF1" wksheet (PAF1!F21) and also in cell B13 of "air" worksheet.

Equation (10):

PM_fil_emssn_PAF1_coal_hrly = max_heat_input_PAF1*PM_fil_emssn_factr_PAF1_coal

PM_fil_emssn_PAF1_coal_hrly = 4.96E+02 lb/unit-hr This value, listed in cell PAF1!G21, is based on average PM_fil emssn factr & Title V max heat-input capacity.

Equation (11):

PM10_fil_emssn_PAF1_coal = PM_fil_emssn_PAF1_coal*PM_fil_sub10_ESP/100

PM10_fil_emssn_PAF1_coal = 1.04E+03 tpy This value is listed in cell PAF1!F22 and also in cell B14 of "air" worksheet.

Equation (12):

PM10_fil_emssn_factr_PAF1_coal = PM10_fil_emssn_PAF1_coal*(2000lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)

PM10_fil_emssn_factr_PAF1_coal = 4.84E-02 lb/MBtu

Equation (13):

PM10_fil_emssn_PAF1_coal_hrly = max_heat_input_PAF1*PM10_fil_emssn_factr_PAF1_coal

Page 1 of 12
calcs

PM10_fil_emssn_PAF1_coal_hrly = 3.37E+02 lb/unit-hr This value, listed in cell PAF1!G22, is based on average PM10_fil emssn factr & Title V max heat-input capacity.

Equation (14):

PM2.5_fil_emssn_PAF1_coal = PM_fil_emssn_PAF1_coal*PM_fil_sub2.5_ESP/100

PM2.5_fil_emssn_PAF1_coal = 5.49E+02 tpy This value is listed in cell PAF1!F23 and also in cell B15 of "air" worksheet.

Equation (15):

PM2.5_fil_emssn_factr_PAF1_coal = PM2.5_fil_emssn_PAF1_coal*(2000lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)

PM2.5_fil_emssn_factr_PAF1_coal = 2.56E-02 lb/MBtu

Equation (16):

PM2.5_fil_emssn_PAF1_coal_hrly = max_heat_input_PAF1*PM2.5_fil_emssn_factr_PAF1_coal

PM2.5_fil_emssn_PAF1_coal_hrly = 1.78E+02 lb/unit-hr This value, listed in cell PAF1!G23, is based on average PM2.5_fil emssn factr & Title V max heat-input capacity.

Equation (17):

PM2.5_fil_EC_emssn_PAF1_coal_hrly = PM2.5_fil_emssn_PAF1_coal_hrly*PM2.5_fil_EC_fractn/100

PM2.5_fil_EC_emssn_PAF1_coal_hrly = 6.60E+00 lb/unit-hr EC fractn of PM2.5_fil emssn, listed in cell AM7 of "BART" worksheet, assigned entirely to smallest CALPUFF size range.

Condensable Particulate Matter (PM_cond)

Equation (1):

PM_cond_emssn_PAF1_coal = heat_input_PAF1_coal*(10^6 MBtu/TBtu)*PM_cond_emssn_factr_coal_FGD*(ton/2000 lb)

PM_cond_emssn_PAF1_coal = 4.28E+02 tpy This value is listed in cell PAF1!F24 and also in cell B16 of "air" worksheet.

Equation (2):

PM_cond_emssn_PAF1_coal_hrly = max_heat_input_PAF1*PM_cond_emssn_factr_coal_FGD

PM_cond_emssn_PAF1_coal_hrly = 1.39E+02 lb/unit-hr This value, listed in cell PAF1!G24, is based on average PM_cond emssn factr & Title V max heat-input capacity.

Equation (3):

PM_cond_org_emssn_PAF1_coal_hrly = PM_cond_emssn_PAF1_coal_hrly*PM_cond_organic_fractn/100

PM_cond_org_emssn_PAF1_coal_hrly = 2.78E+01 lb/unit-hr Organic portion of PM_cond emssn, equally apportioned between cells Y7 and Z7 in "BART" worksheet

AP-42 indicates that all condensable-PM particles are presumed to be less than 1 micron in diameter. PM_cond emissions were assumed to be split equally between the 2 submicron CALPUFF particle-size ranges. 6

Filterable-PM Particle-Size Speciation

Equation (1):

PM10_fil_fractn_6_10 = (PM_fil_sub10_ESP - PM_fil_sub6_ESP)/PM_fil_sub10_ESP*100

PM10_fil_fractn_6_10 = 17.6 % Fraction (%) of PM10_fil in size range between 6 and 10 micrometers

Equation (2):

PM10_fil_fractn_2.5_6 = (PM_fil_sub6_ESP - PM_fil_sub2.5_ESP)/PM_fil_sub10_ESP*100

PM10_fil_fractn_2.5_6 = 29.4 % Fraction (%) of PM10_fil in size range between 2.5 and 6 micrometers

Equation (3):

PM10_fil_fractn_1.25_2.5 = (PM_fil_sub2.5_ESP - PM_fil_sub1.25_ESP)/PM_fil_sub10_ESP*100

PM10_fil_fractn_1.25_2.5 = 20.6 % Fraction (%) of PM10_fil in size range between 1.25 and 2.5 micrometers

Equation (4):

PM10_fil_fractn_1_1.25 = (PM_fil_sub1.25_ESP - PM_fil_sub1_ESP)/PM_fil_sub10_ESP*100

PM10_fil_fractn_1_1.25 = 7.4 % Fraction (%) of PM10_fil in size range between 1 and 1.25 micrometer

Equation (5):

PM10_fil_fractn_sub1 = (PM_fil_sub1_ESP)/PM_fil_sub10_ESP*100

PM10_fil_fractn_sub1 = 25.0 % AP-42 cyclone-boiler PM_fil particle-size distributn contains no data for size range < 0.625 micrometer.

Equation (6):

PM10_fil_fractn_6_10_emssn_PAF1_coal_hrly = PM10_fil_emssn_PAF1_coal_hrly*PM10_fil_fractn_6_10/100

PM10_fil_fractn_6_10_emssn_PAF1_coal_hrly = 5.95E+01 lb/unit-hr This value, listed in cell BART!AD7, is presumed to consist entirely of soil (flyash) components.

Equation (7):

PM10_fil_fractn_2.5_6_emssn_PAF1_coal_hrly = PM10_fil_emssn_PAF1_coal_hrly*PM10_fil_fractn_2.5_6/100

PM10_fil_fractn_2.5_6_emssn_PAF1_coal_hrly = 9.91E+01 lb/unit-hr This value, listed in cell BART!AE7, is presumed to consist entirely of soil (flyash) components.

Equation (8):

PM10_fil_fractn_1.25_2.5_emssn_PAF1_coal_hrly = PM10_fil_emssn_PAF1_coal_hrly*PM10_fil_fractn_1.25_2.5/100

PM10_fil_fractn_1.25_2.5_emssn_PAF1_coal_hrly = 6.94E+01 lb/unit-hr This value, listed in cell BART!AF7, is presumed to consist entirely of soil (flyash) components.

Equation (9):

PM10_fil_fractn_1_1.25_emssn_PAF1_coal_hrly = PM10_fil_emssn_PAF1_coal_hrly*PM10_fil_fractn_1_1.25/100

PM10_fil_fractn_1_1.25_emssn_PAF1_coal_hrly = 2.48E+01 lb/unit-hr This value, listed in cell BART!AG7, is presumed to consist entirely of soil (flyash) components.

Equation (10):

PM10_fil_sub1_emssn_PAF1_coal_hrly = PM10_fil_emssn_PAF1_coal_hrly*PM10_fil_fractn_sub1/100

PM10_fil_sub1_emssn_PAF1_coal_hrly = 8.43E+01 lb/unit-hr

Equation (11):

PM10_fil_sub1_flyash_emssn_PAF1_coal_hrly = PM10_fil_sub1_emssn_PAF1_coal_hrly - PM2.5_fil_EC_emssn_PAF1_coal_hrly

PM10_fil_sub1_flyash_emssn_PAF1_coal_hrly = 7.77E+01 lb/unit-hr Submicron PM_fil minus elemental carbon (EC) = soil (flyash) components, listed in cell BART!AH7

Submicron PM_fil soil (flyash) components were assigned to the 0.625-to-1 micrometer CALPUFF size range, based on cyclone coal-fired boiler PM-speciation guidance posted on the National Park Service (NPS) website. 35

Carbon Monoxide (CO)

Equation (1):

CO_emssn_PAF1_coal = coal_burn_PAF1*CO_uncontrlld_emissn_factr_coal*(ton/2000 lb)

CO_emssn_PAF1_coal = 4.67E+02 tpy This value is listed in cell PAF1!F27 and also in cell B19 of "air" worksheet.

Equation (2):

CO_emssn_factr_PAF1_coal = CO_emssn_PAF1_coal*(2000lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)

CO_emssn_factr_PAF1_coal = 2.18E-02 lb/MBtu

Equation (3):

CO_emssn_PAF1_coal_hrly = max_heat_input_PAF1*CO_emssn_factr_PAF1_coal

CO_emssn_PAF1_coal_hrly = 1.52E+02 lb/unit-hr This value, listed in cell PAF1!G27, is based on average CO emssn factr & Title V max heat-input capacity.

Volatile Organic Compounds (VOC)

Equation (1):

VOC_emssn_PAF1_coal = coal_burn_PAF1*VOC_uncontrlld_emissn_factr_coal*(ton/2000 lb)

VOC_emssn_PAF1_coal = 1.03E+02 tpy This value is listed in cell PAF1!F28 and also in cell B20 of "air" worksheet.

Equation (2):

VOC_emssn_factr_PAF1_coal = VOC_emssn_PAF1_coal*(2000lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)

VOC_emssn_factr_PAF1_coal = 4.79E-03 lb/MBtu

Equation (3):

VOC_emssn_PAF1_coal_hrly = max_heat_input_PAF1*VOC_emssn_factr_PAF1_coal

VOC_emssn_PAF1_coal_hrly = 3.34E+01 lb/unit-hr This value, listed in cell PAF!G28, is based on average VOC emssn factr & Title V max heat-input capacity.

No sample calculations are needed for annual coal-fired boiler SO2 and NOx emission estimates since they are based on CEMS measurements. The following explains hourly SO2 and NOx emission estimates.

Sulfur Dioxide (SO2)

Equation (1):

SO2_emssn_factr_PAF1_CEMS = SO2_emssn_PAF1_CEMS*(2000 lb/ton)/heat_input_PAF1_CEMS

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SO2_emssn_factr_PAF1_CEMS = 6.28E-01 lb/MBtu

Equation (2):

SO2_emssn_PAF1_coal_hrly = max_heat_input_PAF1*SO2_emssn_factr_PAF1_CEMS

SO2_emssn_PAF1_coal_hrly = 4.37E+03 lb/unit-hr This value, listed in cell PAF1!G25, is based on CY05-average CEMS SO2 emssn factr & Title V max heat-input capacity.

Nitrogen Oxides (NOx)

Equation (1):

NOx_emssn_factr_PAF1_CEMS = NOx_emssn_PAF1_CEMS*(2000 lb/ton)/heat_input_PAF1_CEMS

NOx_emssn_factr_PAF1_CEMS = 5.31E-01 lb/MBtu

Equation (2):

NOx_emssn_PAF1_coal_hrly = max_heat_input_PAF1*NOx_emssn_factr_PAF1_CEMS

NOx_emssn_PAF1_coal_hrly = 3.69E+03 lb/unit-hr This value, listed in cell PAF1!G26, is based on CY05-average CEMS NOx emssn factr & Title V max heat-input capacity.

PAF Unit 1 Routine Coal-fired Sulfur Trioxide (SO3)/Sulfuric Acid (H2SO4) Emission Estimates

General Input Variables: Value Units Notes Reference

bitum_S_to_SOx = 95 % Bituminous coal-sulfur conversion to sulfur oxides (SOx) 12

subbit_S_to_SOx = 87.5 % Subbituminous coal-sulfur conversion to sulfur oxides (SOx) 12

SO3_to_SO2_molar_ratio_EB = 1.6 % SO3/SO2 ratio for cyclone-fired boilers burning Eastern bituminous (EB) coals 12

SO3_to_SO2_molar_ratio_WB = 0.22 % SO3/SO2 ratio for cyclone-fired boilers burning Western bituminous (WB) coals 12

SO3_to_SO2_molar_ratio_Sub = 0.3 % SO3/SO2 ratio for cyclone-fired boilers burning subbituminous (Sub) coals 12

AH_SO3_contrl_effncy_LSE = 51 % SO3 control efficiency for air heaters (AH) in units burning low-sulfur (<2.5% S) Eastern (LSE) bitum. coals 12

AH_SO3_contrl_effncy_HSE = 15 % SO3 control efficiency for air heaters (AH) in units burning high-sulfur (>=2.5% S) Eastern (HSE) bitum. coals 12

AH_SO3_contrl_effncy_WC = 10 % SO3 control efficiency for AH in units burning W. bitum. & subbit. (WC) coals 12

ESP_SO3_contrl_effncy_LSE = 51 % SO3 control efficiency for cold-side electrostatic precipitators (ESP) in units burning low-S E. bitum. (LSE) coals 12

ESP_SO3_contrl_effncy_HSE = 23 % SO3 control efficiency for cold-side ESP in units burning high-S E. bitum. (HSE) coals 12

ESP_SO3_contrl_effncy_WC = 50 % SO3 control efficiency for cold-side ESP in units burning W. bitum. & subbit. (WC) coals 12

BF_SO3_contrl_effncy = 90 % SO3 control efficiency for bagfilters (BF) 12

WST_SO3_contrl_effncy_EB = 53 % SO3 control efficiency for wet spray tower (WST) FGD scrubbers in units burning Eastern bitum. (EB) coals 12

WST_SO3_contrl_effncy_WC = 60 % SO3 control efficiency for WST FGD scrubbers in units burning Western bitum. & subbitum. (WC) coals 12

WV_SO3_contrl_effncy = 35 % SO3 control efficiency for wet venturi (WV) FGD scrubbers 12

Dry_FGD_BF_SO3_contrl_effncy = 99 % SO3 control efficiency for dry flue-gas-desulfurization (FGD) scrubbers with downstream bagfilter controls 12

H2SO4_to_SO3_molar_ratio = 100 % Assume all SO3 converted to H2SO4 downstrm of air heater 12

flue_gas_factr_dry = 9,780 dry std ft^3/MBtu Dry flue-gas factor for bitum & subbit. coals at 0% excess air 12

flue_gas_factr_wet_0%O2 = 10,640 wet std ft^3/MBtu Wet flue-gas factor for bitum & subbit. coals at 0% excess air 12

flue_gas_O2_concen = 3 %-volume (dry basis) Flue-gas O2 concentration used as standard for TVA test measurements (typical coal-fired AH-inlet O2 level)

SO2_conv_factr = 1.66E-07 (lb/std ft^3)/ppmv SO2 factor to convert from mass/volume concentration to parts per million by volume (ppmv) 12

H2SO4_conv_factr = 2.54E-07 (lb/std ft^3)/ppmv H2SO4 factor to convert from mass/volume concentration to ppmv 12

S_mol_wt = 32.064 lb/lb-mole Sulfur (S) molecular weight 11

SO2_mol_wt = 64.0628 lb/lb-mole Sulfur dioxide (SO2) molecular weight 11

H2SO4_mol_wt = 98.0774 lb/lb-mole Sulfuric acid (H2SO4) molecular weight 11

blr_operatn_hrs_PAF1 = 7,397 hours/year (hr/yr) PAF Unit 1 boiler total in-service hours 2

SCR_operatn_hrs_PAF1 = 3586 hr/yr PAF Unit 1 selective-catalytic-reduction (SCR) reactor total in-service hours (in flue-gas path) 13

SCR_NH3_operatn_hrs_PAF1 = 3185 hr/yr PAF Unit 1 SCR reactor in-service hours (with ammonia [NH3] feed) 13

SCR_SO2_oxidatn_rate = 0.75 % PAF design SCR-reactor catalyst SO2 oxidation rate 14

NH3_slip = 2 ppmv on dry basis (ppmvd) Vendor-guaranteed maximum SCR-exit dry flue-gas NH3 concentration (slip) at 20,000 SCR operating hours 15

molar_vol_STP = 359.036 ft^3/lb-mole at STP Molar volume of gas at temperature = 0 deg C and pressure = 760 mm Hg (ideal-gas-law equation) 12

flue_gas_SO3_concen_stk_PAF_SCR_byp_FGD = 14.2 ppmvd at 3% O2 CY05 test data for PAF Unit 2 stack-exit SO3/H2SO4 dry flue-gas concentration with bypassed SCR reactor 16

flue_gas_SO3_concen_stk_PAF_SCR_FGD = 17.7 ppmvd at 3% O2 CY05 test data for PAF Unit 2 stack-exit SO3/H2SO4 dry flue-gas concentration with in-service SCR reactor 16

Coal-fired Boiler Combustion-Derived SO3/H2SO4 Manufacture/Emission Estimates (HSD Method):

PAF Unit 1 Illinois Basin (ILB) bituminous coal:

Equation (1):

Blr_exit_SOx_PAF1_ILB = coal_burn_PAF1_ILB*coal_S_PAF_ILB/100*bitum_S_to_SOx/100*SO2_mol_wt/S_mol_wt

Blr_exit_SOx_PAF1_ILB = 9.43E+04 tpy

Equation (2):

Blr_H2SO4_productn_PAF1_ILB = Blr_exit_SOx_PAF1_ILB*SO3_to_SO2_molar_ratio_EB/100*H2SO4_to_SO3_molar_ratio*H2SO4_mol_wt/SO2_mol_wt 

Blr_H2SO4_productn_PAF1_ILB = 2.31E+03 tpy

Equation (3):

Blr_H2SO4_emssn_PAF1_ILB = Blr_H2SO4_productn_PAF1_ILB*(1-AH_SO3_contrl_effncy_EB/100)*(1-WV_SO3_contrl_effncy/100)

Blr_H2SO4_emssn_PAF1_ILB = 1.28E+03 tpy PAF Unit 1 ILB-coal boiler combustion-derived contributn to SO3/H2SO4 stack emissns (HSD Method)

PAF Unit 1 Powder River Basin (PRB) subbituminous coal:

Equation (4):

Blr_exit_SOx_PAF1_PRB = coal_burn_PAF1_PRB*coal_S_PAF_PRB/100*subbit_S_to_SOx/100*SO2_mol_wt/S_mol_wt

Blr_exit_SOx_PAF1_PRB = 1.14E+02 tpy

Equation (5):

Blr_H2SO4_productn_PAF1_PRB = Blr_exit_SOx_PAF1_PRB*SO3_to_SO2_molar_ratio_sub/100*H2SO4_to_SO3_molar_ratio*H2SO4_mol_wt/SO2_mol_wt 

Blr_H2SO4_productn_PAF1_PRB = 5.22E-01 tpy

Equation (6):

Blr_H2SO4_emssn_PAF1_PRB = Blr_H2SO4_productn_PAF1_PRB*(1-AH_SO3_contrl_effncy_WC/100)*(1-WV_SO3_contrl_effncy/100)

Blr_H2SO4_emssn_PAF1_PRB = 3.06E-01 tpy PAF Unit 1 PRB-coal boiler combustion-derived contributn to SO3/H2SO4 stack emissns (HSD Method)

PAF Unit 1 total-coal boiler combustion-derived SO3/H2SO4 emssn:

Equation (7):

Blr_H2SO4_productn_PAF1_coal = Blr_H2SO4_productn_PAF1_ILB+Blr_H2SO4_productn_PAF1_PRB

Blr_H2SO4_productn_PAF1_coal = 2.31E+03 tpy

Equation (8):

Blr_H2SO4_emssn_PAF1_coal = Blr_H2SO4_emssn_PAF1_ILB+Blr_H2SO4_emssn_PAF1_PRB

Blr_H2SO4_emssn_PAF1_coal = 1.28E+03 tpy PAF Unit 1 coal-fired blr combustn-derived contributn to SO3/H2SO4 emissns (HSD method)--not used for CY05 estimates

Equation (9):

Blr_H2SO4_contrl_effncy_PAF1 = (1-Blr_H2SO4_emssn_PAF1_coal/Blr_H2SO4_productn_PAF1_coal)*100

Blr_H2SO4_contrl_effncy_PAF1 = 44.75 %

Equation (10):

Blr_H2SO4_flue_gas_concen_PAF1 = Blr_H2SO4_emssn_PAF1_coal*(2000 lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)/flue_gas_factr_dry*(20.9-flue_gas_O2_concen)/20.9/H2SO4_conv_factr

Blr_H2SO4_flue_gas_concen_PAF1 = 2.06E+01 ppmvd Coal-fired blr combustion-derived contributn to PAF Unit 1 stk-exit SO3/H2SO4 flue-gas concentration (HSD Method).

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Selective-catalytic-reduction (SCR) Reactor-Derived SO3/H2SO4 Emission Estimates (HSD Method):

PAF Unit 1 Illinois Basin (ILB) bituminous coal:

Equation (1):

SCR_oper_factr_PAF1 = SCR_operatn_hrs_PAF1/blr_operatn_hrs_PAF1

SCR_oper_factr_PAF1 = 4.85E-01 (dimensionless) Nominal fraction of PAF Unit 1 coal burn while SCR reactor was in flue-gas path

Equation (2):

SCR_H2SO4_productn_PAF1_ILB = Blr_exit_SOx_PAF1_ILB*SCR_SO2_oxidatn_rate/100*SCR_oper_factr_PAF1*H2SO4_mol_wt/SO2_mol_wt 

SCR_H2SO4_productn_PAF1_ILB = 5.25E+02 tpy

Equation (3):

SCR_NH3_oper_factr_PAF1 = SCR_NH3_operatn_hrs_PAF1/blr_operatn_hrs_PAF1

SCR_NH3_oper_factr_PAF1 = 4.31E-01 (dimensionless) Fraction of PAF Unit 1 coal burn while SCR reactor was in flue-gas path with NH3 inputs

Equation (4):

NH3_neutrlztn_PAF1_ILB = heat_input_PAF1_ILB*(10^6 MBtu/TBtu)*SCR_NH3_oper_factr_PAF1*flue_gas_factr_dry*20.9/(20.9-flue_gas_O2_concen)*NH3_slip/(molar_vol_STP*293.15/273.15)*H2SO4_mol_wt*(ton/2000 lb)

NH3_neutrlztn_PAF1_ILB = 5.36E+01 tpy PAF Unit 1 ILB-coal-fired SO3/H2SO4 quantity neutralized by NH3 slip.

Equation (5):

SCR_H2SO4_emssn_PAF1_ILB = (SCR_H2SO4_productn_PAF1_ILB-NH3_neutrlztn_PAF1_ILB)*(1-AH_SO3_contrl_effncy_EB/100)*(1-WV_SO3_contrl_effncy/100)

SCR_H2SO4_emssn_PAF1_ILB = 2.61E+02 tpy PAF Unit 1 ILB-coal-fired boiler SCR-derived contributn to SO3/H2SO4 stack emissns (HSD Method)

PAF Unit 1 Powder River Basin (PRB) subbituminous coal:

Equation (6):

SCR_H2SO4_productn_PAF1_PRB = Blr_exit_SOx_PAF1_PRB*SCR_SO2_oxidatn_rate/100*SCR_oper_factr_PAF1*H2SO4_mol_wt/SO2_mol_wt 

SCR_H2SO4_productn_PAF1_PRB = 6.33E-01 tpy H2SO4

Equation (7):

NH3_neutrlztn_PAF1_PRB = heat_input_PAF1_PRB*(10^6 MBtu/TBtu)*SCR_NH3_oper_factr_PAF1*flue_gas_factr_dry*20.9/(20.9-flue_gas_O2_concen)*NH3_slip/10^6/(molar_vol_STP*293.15/273.15)*H2SO4_mol_wt*(ton/2000 lb)

NH3_neutrlztn_PAF1_PRB = 4.08E-01 tpy H2SO4 PAF Unit 1 PRB-coal-fired SO3/H2SO4 quantity neutralized by NH3 slip.

Equation (8):

SCR_H2SO4_emssn_PAF1_PRB = (SCR_H2SO4_productn_PAF1_PRB-NH3_neutrlztn_PAF1_PRB)*(1-AH_SO3_contrl_effncy_WC/100)*(1-WV_SO3_contrl_effncy/100)

SCR_H2SO4_emssn_PAF1_PRB = 1.32E-01 tpy H2SO4 PAF Unit 1 PRB-coal-fired boiler SCR-derived contributn to SO3/H2SO4 stack emissns (HSD Method)

PAF Unit 1 Total-coal SCR-derived SO3/H2SO4 Emission Estimate:

Equation (9):

SCR_H2SO4_productn_PAF1_coal = SCR_H2SO4_productn_PAF1_ILB + SCR_H2SO4_productn_PAF1_PRB

SCR_H2SO4_productn_PAF1_coal = 5.26E+02 tpy H2SO4

Equation (10):

SCR_H2SO4_emssn_PAF1_coal = SCR_H2SO4_emssn_PAF1_ILB + SCR_H2SO4_emssn_PAF1_PRB

SCR_H2SO4_emssn_PAF1_coal = 2.61E+02 tpy H2SO4 SCR-derived contributn to PAF Unit 1 SO3/H2SO4 stk emissions, per HSD method (not used for CY05 estimates) 

Equation (11):

SCR_H2SO4_contrl_effncy_PAF1_coal = (1-SCR_H2SO4_emssn_PAF1_coal/SCR_H2SO4_productn_PAF1_coal)*100

SCR_H2SO4_contrl_effncy_PAF1_coal = 50.42 %

Equation (12):

SCR_H2SO4_flue_gas_concen_PAF1 = SCR_H2SO4_emssn_PAF1_coal*(2000 lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)/flue_gas_factr_dry*(20.9-flue_gas_O2_concen)/20.9/H2SO4_conv_factr

SCR_H2SO4_flue_gas_concen_PAF1 = 4.20E+00 ppmvd SCR-derived contributn to annual-average PAF Unit 1 flue-gas SO3/H2SO4 concentration (HSD Method).

PAF Unit 1 Total Coal-fired SO3/H2SO4 Emission Estimates (HSD Method):

Equation (1):

H2SO4_productn_PAF1_coal_HSD = Blr_H2SO4_productn_PAF1_coal+SCR_H2SO4_productn_PAF1_coal

H2SO4_productn_PAF1_coal_HSD = 2.84E+03 tpy

Equation (2):

H2SO4_emssn_PAF1_coal_HSD = Blr_H2SO4_emssn_PAF1_coal+SCR_H2SO4_emssn_PAF1_coal

H2SO4_emssn_PAF1_coal_HSD = 1.54E+03 tpy PAF Unit 1 coal-fired blr- & SCR-derived contributn to SO3/H2SO4 emissns (HSD method)--not used for CY05 estimates.

Equation (3):

H2SO4_contrl_effncy_PAF1_coal_HSD = (1-H2SO4_emssn_PAF1_coal/H2SO4_productn_PAF1_coal)*100

H2SO4_contrl_effncy_PAF1_coal_HSD = 45.80 %

Equation (4):

H2SO4_stk_gas_concen_PAF1_coal_HSD = H2SO4_emssn_PAF1_coal*(2000 lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)/flue_gas_factr_dry*(20.9-flue_gas_O2_concen)/20.9/H2SO4_conv_factr

H2SO4_stk_gas_concen_PAF1_coal_HSD = 2.48E+01 ppmvd PAF Unit 1 total SO3/H2SO4 stack-exit flue-gas concentration (HSD Method).

PAF Unit 1 Total Coal-fired SO3/H2SO4 Emission Estimates (Flue-Gas-Concentration Method):

Equation (1):

flue_gas_SO3_concen_stk_exit_PAF1_avg = flue_gas_SO3_concen_stk_PAF_SCR_byp_FGD*(1-SCR_oper_factr_PAF1)+flue_gas_SO3_concen_stk_PAF_SCR_FGD*SCR_oper_factr_PAF1

flue_gas_SO3_concen_stk_exit_PAF1_avg = 1.59E+01 ppmvd at 3% O2

Equation (2):

H2SO4_emssn_PAF1_coal = heat_input_PAF1_coal*(10^6 MBtu/TBtu)*flue_gas_factr_dry*20.9/(20.9-flue_gas_O2_concen)*flue_gas_SO3_concen_stk_exit_PAF1_avg*H2SO4_conv_factr*(ton/2000 lb)

H2SO4_emssn_PAF1_coal = 9.88E+02 tpy H2SO4 PAF Unit 1 coal-fired blr- & SCR-derived contributn to SO3/H2SO4 emissns, listed in PAF1!F29 and in air!B21.

Equation (3):

H2SO4_emssn_factr_PAF1_coal = H2SO4_emssn_PAF1_coal*(2000lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)

H2SO4_emssn_factr_PAF1_coal = 4.61E-02 lb/MBtu

Equation (4):

H2SO4_emssn_PAF1_coal_hrly = max_heat_input_PAF1*H2SO4_emssn_factr_PAF1_coal

H2SO4_emssn_PAF1_coal_hrly = 3.21E+02 lb/unit-hr This value, listed in cell PAF1!G29, is based on average H2SO4 emssn factr & Title V max heat-input capacity.

Equation (5):

H2SO4_contrl_effncy_PAF1_coal = (1-H2SO4_emssn_PAF1_coal/H2SO4_productn_PAF1_coal_HSD)*100

H2SO4_contrl_effncy_PAF1_coal = 65.18 %

PAF Unit 1 Routine CY05 Ammonia (NH3) Emission Estimates

General Input Variables: Value Units Notes Reference

blr_operatn_hrs_PAF1 = 7,397 hours/year (hr/yr) PAF Unit 1 boiler total in-service hours 2

blr_operatn_hrs_PAF2 = 8,452 hr/yr PAF Unit 2 boiler total in-service hours 2

blr_operatn_hrs_PAF3 = 5,705 hr/yr PAF Unit 3 boiler total in-service hours 2

SCR_NH3_operatn_hrs_PAF1 = 3,185 hr/yr PAF Unit 1 selective-catalytic-reduction (SCR) reactor total in-service hours (with NH3 inputs) 13

SCR_NH3_operatn_hrs_PAF2 = 3,811 hr/yr PAF Unit 2 SCR reactor total in-service hours (with NH3 inputs) 13

SCR_NH3_operatn_hrs_PAF3 = 3,072 hr/yr PAF Unit 3 SCR reactor total in-service hours (with NH3 inputs) 13

flue_gas_factr_wet_3%O2 = 12,423 wet std ft^3/MBtu Wet flue-gas factor for bitum & subbit. coals at 3% O2 flue-gas concentratn (typical SCR-inlet O2 concentratn) 17

molar_vol = 385.5 std ft^3/lb-mol Ideal-gas-law (PV = nRT) molar volume at 20 deg C (68 deg F) 17

NH3_slip = 2 ppmv on dry basis (ppmvd) Vendor-guaranteed maximum SCR-exit dry flue-gas NH3 concentration (slip) at 20,000 SCR operating hours 15

NH3_mol_wt = 17.0304 lb/lb-mole Ammonia (NH3) molecular weight 11

anhydrous_NH3_recpts_truck = 988,000 lb/yr CY05 PAF anhydrous NH3 receipts by truck 18

anhydrous_NH3_recpts_rail = 18,800,924 lb/yr CY05 PAF anhydrous NH3 receipts by rail 18

unloading_emssn_factr_truck_NH3 = 1.38E-05 lb/lb NH3 delivery Emission factor estimated from pipe/hose dimensions/volumes for truck deliveries at TVA's Paradise Fossil Plant 19

unloading_emssn_factr_rail_NH3 = 1.05E-07 lb/lb NH3 delivery Emission factor estimated from pipe/hose dimensions/volumes for rail deliveries at TVA's Paradise Fossil Plant 19

T1_AH_EB = 0.001 dimensionless Penetration of gaseous NH3 through air heater (AH) in units burning Eastern bituminous (EB) coal 17

T1_CS_ESP_EB = 1.00 dimensionless Penetration of gaseous NH3 through cold-side electrostatic precipitator (CS ESP) in units burning EB coal 17

Page 4 of 12
calcs

T1_BF_EB = 0.10 dimensionless Penetration of gaseous NH3 through bagfilter (BF) in units burning EB coal 17

T1_WFGD_EB = 0.01 dimensionless Penetration of gaseous NH3 through wet flue-gas-desulfurization (WFGD) scrubber in units burning EB coal 17

T1_DFGD_BF_EB = 0.025 dimensionless Penetration of gaseous NH3 through dry FGD scrubber with bagfilter (DFGD_BF) in units burning EB coal 17

T1_AH_PRB = 0.75 dimensionless Penetration of gaseous NH3 through AH in units burning PRB subbituminous coal 17

T1_POST_APH_FGC_PRB = 0.35 dimensionless Penetration of gaseous NH3 through post-AH SO3 flue-gas-conditioning (FGC) in units burning PRB subbit. coal 17

T1_CS_ESP_PRB = 1.00 dimensionless Penetration of gaseous NH3 through CS ESP in units burning PRB subbituminous coal 17

T1_BF_PRB = 0.95 dimensionless Penetration of gaseous NH3 through BF in units burning PRB subbituminous coal 17

T1_WFGD_PRB = 0.01 dimensionless Penetration of gaseous NH3 through WFGD scrubber in units burning PRB subbituminous coal 17

T1_DFGD_BF_PRB = 0.2375 dimensionless Penetration of gaseous NH3 through DFGD scrubber with BF in units burning PRB subbituminous coal 17

T1_AH_RMB = 0.56275 dimensionless Penetration of gaseous NH3 through AH in units burning Rocky Mtn bituminous (RMB) coal 20

T1_POST_APH_FGC_RMB = 0.26275 dimensionless Penetration of gaseous NH3 through post-AH SO3 FGC in units burning RMB coal 20

T1_CS_ESP_RMB = 1.00 dimensionless Penetration of gaseous NH3 through CS ESP in units burning RMB coal 20

T1_BF_RMB = 0.7375 dimensionless Penetration of gaseous NH3 through BF in units burning RMB coal 20

T1_WFGD_RMB = 0.01 dimensionless Penetration of gaseous NH3 through WFGD scrubber in units burning RMB coal 20

T1_DFGD_BF_RMB = 0.184375 dimensionless Penetration of gaseous NH3 through DFGD scrubber with BF in units burning RMB coal 20

T5_AH_EB = 0.75 dimensionless Fraction of NH3 adsorbed on particles (and NH4 salts) & penetrating AH in units burning EB coal 17

T5_AH_FGC_PRB = 0.60 dimensionless Fraction of NH3 adsorbed on particles (and NH4 salts) & penetrating AH in units burning PRB coal w/ SO3 FGC 17

T5_AH_PRB = 0.20 dimensionless Fraction of NH3 adsorbed on particles (and NH4 salts) & penetrating AH in units burning PRB coal 17

T5_AH_FGC_RMB = 0.6375 dimensionless Fraction of NH3 adsorbed on particles (and NH4 salts) & penetrating AH in units burning RMB coal w/ SO3 FGC 20

T5_AH_RMB = 0.3375 dimensionless Fraction of NH3 adsorbed on particles (and NH4 salts) & penetrating AH in units burning RMB coal 20

T6_CS_ESP = 0.01 dimensionless Penetration of NH3 adsorbed on particles (and NH4 salts) through CS ESP in units burning any coal 17

T6_BF = 0.002 dimensionless Penetration of NH3 adsorbed on particles (and NH4 salts) through bagfilter in units burning any coal 17

T6_DFGD = 1.00 dimensionless Penetration of NH3 adsorbed on particles (and NH4 salts) through dry FGD scrubber in units burning any coal 17

T6_WFGD = 0.50 dimensionless Penetration of NH3 adsorbed on particles (and NH4 salts) through wet FGD scrubber in units burning any coal 17

T6_WFGD_PAF1_2 = 0.038 dimensionless CY05 penetration of filterable particulate matter (PM_fil) through PAF Units 1-2 venturi wet FGD scrubbers

T7_AH_EB = 0.0490 dimensionless Capture of NH3 adsorbed on particles (and NH4 salts) by AH in units burning EB coal 17

T7_AH_PRB = 0.005 dimensionless Capture of NH3 adsorbed on particles (and NH4 salts) by AH in units burning PRB coal 17

T7_AH_RMB = 0.016 dimensionless Capture of NH3 adsorbed on particles (and NH4 salts) by AH in units burning RMB coal 20

E1_AH_EB_air = 0.20 dimensionless Fugitive air-release fraction of NH3 adsorbed on particles (& NH4 salts) captured by AH in units burning EB coal 17

E1_CS_ESP_EB_air = 0.10 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by CS ESP in units burning EB coal 17

E1_BF_EB_air = 0.10 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by BF in units burning EB coal 17

E1_WFGD_EB_air = 0.20 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by WFGD in units burning EB coal 17

E1_DFGD_BF_EB_air = 0.10 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by DFGD/BF in units burning EB coal 17

E1_AH_PRB_air = 0.95 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by AH in units burning PRB coal 17

E1_CS_ESP_PRB_air = 0.95 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by CS ESP in units burning PRB coal 17

E1_BF_PRB_air = 0.95 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by BF in units burning PRB coal 17

E1_WFGD_PRB_air = 0.95 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by WFGD in units burning PRB coal 17

E1_DFGD_BF_PRB_air = 0.10 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by DFGD/BF in units burning PRB coal 17

E1_AH_RMB_air = 0.7625 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by AH in units burning RMB coal 20

E1_CS_ESP_RMB_air = 0.7375 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by CS ESP in units burning RMB coal 20

E1_BF_RMB_air = 0.7375 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by BF in units burning RMB coal 20

E1_WFGD_RMB_air = 0.7625 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by WFGD in units burning RMB coal 20

E1_DFGD_BF_RMB_air = 0.10 dimensionless Fug. air-release fractn of NH3 adsorbed on particles (& NH4 salts) captured by DFGD/BF in units burning RMB coal 20

aqueous_NH3_rcpts = 44,460 lb/yr PAF plant-total boiler-water-treatment (BWT) aqueous NH3 receipts 18

aqueous_NH3_wt_fractn = 35 % Unless otherwise indicated, presumed weight percent NH3 in BWT aqueous NH3 solution 

BWT_tank_NH3_air = 0.64 dimensionless Fugitive air-release fractn of NH3 in BWT solution disposed to open-air tank 17

BWT_pond_NH3_air = 0.10 dimensionless Fugitive air-release fractn of NH3 in BWT solution disposed to ash pond (PAF uses ash pond for BWTdisposal) 17

FA_productn = 125,672 tons/yr (tpy) PAF flyash production 5

FA_dry_sales = 0 tpy No CY05 PAF dry flyash sales (e.g., off-site cement substitute in ready-mix concrete) 5

Selective-catalytic-reduction (SCR) Reactor-Derived Stack NH3 (& Ammonium Salt) Emission Estimates:

PAF Illinois Basin (ILB) coal:

Equation (1):

SD = FA_dry_sales/FA_productn

SD = 0.00 dimensionless Fraction of fly ash captured dry and sold/transferred offsite

Equation (2):

coal_burn_PAF1_ILB_SCR = coal_burn_PAF1_ILB*SCR_NH3_operatn_hrs_PAF1/blr_operatn_hrs_PAF1

coal_burn_PAF1_ILB_SCR = 795,712 tpy PAF Unit 1 ILB coal burn while SCR reactor was receiving NH3 inputs

Equation (3):

coal_burn_PAF2_ILB_SCR = coal_burn_PAF2_ILB*SCR_NH3_operatn_hrs_PAF2/blr_operatn_hrs_PAF2

coal_burn_PAF2_ILB_SCR = 946,174 tpy

Equation (4):

coal_burn_PAF1_2_ILB_SCR = coal_burn_PAF1_ILB_SCR+coal_burn_PAF2_ILB_SCR

coal_burn_PAF1_2_ILB_SCR = 1,741,886 tpy

Equation (5):

flue_gas_flow_PAF1_2_ILB_SCR = coal_burn_PAF1_2_ILB_SCR*(2000lb/ton)*coal_heat_PAF_ILB*(MBtu/10^6 Btu)*flue_gas_factr_wet_3%O2

flue_gas_flow_PAF1_2_ILB_SCR = 4.98E+11 std ft^3/yr

Equation (6):

SCR_exit_NH3_mass_rate_PAF1_2_ILB = flue_gas_flow_PAF_1_2_ILB_SCR*NH3_slip/10^6*flue_gas_factr_dry/flue_gas_factr_wet_0%O2/molar_vol*NH3_mol_wt

SCR_exit_NH3_mass_rate_PAF1_2_ILB = 4.04E+04 lb/yr

Equation (7):

NH3_stk_emssn_PAF1_2_ILB = SCR_exit_NH3_mass_rate_PAF1_2_ILB*T1_AH_EB*T1_WFGD_EB

NH3_stk_emssn_PAF1_2_ILB = 4.04E-01 lb/yr

Equation (8):

NH4_salt_stk_emssn_PAF1_2_ILB = SCR_exit_NH3_mass_rate_PAF1_2_ILB*T5_AH_EB*T6_WFGD_PAF1_2

NH4_salt_stk_emssn_PAF1_2_ILB = 1.14E+03 lb/yr NH4-salt mass expressed as NH3 equivalent, but subsumed within total PM emissions & not separately reported.

Equation (9):

SCR_NH3_fugitive_emssn_PAF1_2_ILB = SCR_exit_NH3_mass_rate_PAF1_2_ILB*(T7_AH_EB*E1_AH_EB_air+T1_AH_EB*(1-T1_WFGD_EB)*E1_WFGD_EB_air+T5_AH_EB*(1-T6_WFGD_PAF1_2)*E1_WFGD_EB_air)

SCR_NH3_fugitive_emssn_PAF1_2_ILB = 6.24E+03 lb/yr

Equation (10):

coal_burn_PAF3_ILB_SCR = coal_burn_PAF3_ILB*SCR_NH3_operatn_hrs_PAF3/blr_operatn_hrs_PAF3

coal_burn_PAF3_ILB_SCR = 401,258 tpy

Equation (11):

flue_gas_flow_PAF3_ILB_SCR = coal_burn_PAF3_ILB_SCR*(2000lb/ton)*coal_heat_PAF_ILB*(MBtu/10^6 Btu)*flue_gas_factr_wet_3%O2

flue_gas_flow_PAF3_ILB_SCR = 1.15E+11 std ft^3/yr

Equation (12):

SCR_exit_NH3_mass_rate_PAF3_ILB = flue_gas_flow_PAF3_ILB_SCR*NH3_slip/10^6*flue_gas_factr_dry/flue_gas_factr_wet_0%O2/molar_vol*NH3_mol_wt

SCR_exit_NH3_mass_rate_PAF3_ILB = 9.31E+03 lb/yr

Equation (13):

NH3_stk_emssn_PAF3_ILB = SCR_exit_NH3_mass_rate_PAF3_ILB*T1_AH_EB*T1_CS_ESP_EB

NH3_stk_emssn_PAF3_ILB = 9.31E+00 lb/yr

Equation (14):

NH4_salt_stk_emssn_PAF3_ILB = SCR_exit_NH3_mass_rate_PAF3_ILB*T5_AH_EB*T6_CS_ESP

NH4_salt_stk_emssn_PAF3_ILB = 6.98E+01 lb/yr

Equation (15):

SCR_NH3_fugitive_emssn_PAF3_ILB = SCR_exit_NH3_mass_rate_PAF3_ILB*(T7_AH_EB*E1_AH_EB_air+T5_AH_EB*[1-T6_CS_ESP]*[1-SD]*E1_CS_ESP_EB_air)

SCR_NH3_fugitive_emssn_PAF3_ILB = 7.83E+02 lb/yr

PAF Powder River Basin (PRB) subbituminous coal:

Page 5 of 12
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Equation (1):

coal_burn_PAF1_PRB_SCR = coal_burn_PAF1_PRB*SCR_NH3_operatn_hrs_PAF1/blr_operatn_hrs_PAF1

coal_burn_PAF1_PRB_SCR = 8,003 tpy

Equation (2):

coal_burn_PAF2_PRB_SCR = coal_burn_PAF2_PRB*SCR_NH3_operatn_hrs_PAF2/blr_operatn_hrs_PAF2

coal_burn_PAF2_PRB_SCR = 13,181 tpy

Equation (3):

coal_burn_PAF1_2_PRB_SCR = coal_burn_PAF1_PRB_SCR+coal_burn_PAF2_PRB_SCR

coal_burn_PAF1_2_PRB_SCR = 21,184 tpy

Equation (4):

flue_gas_flow_PAF1_2_PRB_SCR = coal_burn_PAF1_2_PRB_SCR*(2000lb/ton)*coal_heat_PAF_PRB*(MBtu/10^6 Btu)*flue_gas_factr_wet_3%O2

flue_gas_flow_PAF1_2_PRB_SCR = 4.62E+09 std ft^3/yr

Equation (5):

SCR_exit_NH3_mass_rate_PAF1_2_PRB = flue_gas_flow_PAF_1_2_PRB_SCR*NH3_slip/10^6*flue_gas_factr_dry/flue_gas_factr_wet_0%O2/molar_vol*NH3_mol_wt

SCR_exit_NH3_mass_rate_PAF1_2_PRB = 3.75E+02 lb/yr

Equation (6):

NH3_stk_emssn_PAF1_2_PRB = SCR_exit_NH3_mass_rate_PAF1_2_PRB*T1_AH_PRB*T1_WFGD_PRB

NH3_stk_emssn_PAF1_2_PRB = 2.81E+00 lb/yr

Equation (7):

NH4_salt_stk_emssn_PAF1_2_PRB = SCR_exit_NH3_mass_rate_PAF1_2_PRB*T5_AH_PRB*T6_WFGD_PAF1_2

NH4_salt_stk_emssn_PAF1_2_PRB = 2.82E+00 lb/yr NH4-salt mass expressed as NH3 equivalent, but subsumed within total PM emissions & not separately reported.

Equation (8):

SCR_NH3_fugitive_emssn_PAF1_2_PRB = SCR_exit_NH3_mass_rate_PAF1_2_PRB*(T7_AH_PRB*E1_AH_PRB_air+T1_AH_PRB*(1-T1_WFGD_PRB)*E1_WFGD_PRB_air+T5_AH_PRB*(1-T6_WFGD_PAF1_2)*E1_WFGD_PRB_air)

SCR_NH3_fugitive_emssn_PAF1_2_PRB = 3.35E+02 lb/yr

Equation (9):

coal_burn_PAF3_PRB_SCR = coal_burn_PAF3_PRB*SCR_NH3_operatn_hrs_PAF3/blr_operatn_hrs_PAF3

coal_burn_PAF3_PRB_SCR = 982,390 tpy

Equation (10):

flue_gas_flow_PAF3_PRB_SCR = coal_burn_PAF3_PRB_SCR*(2000lb/ton)*coal_heat_PAF_PRB*(MBtu/10^6 Btu)*flue_gas_factr_wet_3%O2

flue_gas_flow_PAF3_PRB_SCR = 2.14E+11 std ft^3/yr

Equation (11):

SCR_exit_NH3_mass_rate_PAF3_PRB = flue_gas_flow_PAF3_PRB_SCR*NH3_slip/10^6*flue_gas_factr_dry/flue_gas_factr_wet_0%O2/molar_vol*NH3_mol_wt

SCR_exit_NH3_mass_rate_PAF3_PRB = 1.74E+04 lb/yr

Equation (12):

NH3_stk_emssn_PAF3_PRB = SCR_exit_NH3_mass_rate_PAF3_PRB*T1_AH_PRB*T1_CS_ESP_PRB

NH3_stk_emssn_PAF3_PRB = 1.30E+04 lb/yr

Equation (13):

NH4_salt_stk_emssn_PAF3_PRB = SCR_exit_NH3_mass_rate_PAF3_PRB*T5_AH_PRB*T6_CS_ESP

NH4_salt_stk_emssn_PAF3_PRB = 3.48E+01 lb/yr

Equation (14):

SCR_NH3_fugitive_emssn_PAF3_PRB = SCR_exit_NH3_mass_rate_PAF3_PRB*(T7_AH_PRB*E1_AH_PRB_air+T5_AH_PRB*[1-T6_CS_ESP]*[1-SD]*E1_CS_ESP_PRB_air)

SCR_NH3_fugitive_emssn_PAF3_PRB = 3.35E+03 lb/yr

PAF Unit 1 Coal-fired Boiler-Total SCR-Reactor-Derived Stack NH3 (& Ammonium Salt) Emission Estimates:

Equation (1):

NH3_stk_emssn_PAF1_coal = (NH3_stk_emssn_PAF1_2_ILB+NH3_stk_emssn_PAF1_2_PRB)*coal_burn_PAF1_ILB_SCR/coal_burn_PAF1_2_ILB_SCR*(ton/2000 lb)

NH3_stk_emssn_PAF1_coal = 7.35E-04 tons/yr (tpy) CY05 PAF Unit 1 gaseous NH3 stack emissions, listed in cell PAF1!F30 and also in cell B22 of "air" worksheet

Equation (2):

NH3_emssn_factr_PAF1_coal = NH3_stk_emssn_PAF1_coal*(2000lb/ton)/heat_input_PAF1_coal*(TBtu/10^6 MBtu)

NH3_emssn_factr_PAF1_coal = 3.43E-08 lb/MBtu

Equation (3):

NH3_emssn_PAF1_coal_hrly = max_heat_input_PAF1*NH3_emssn_factr_PAF1_coal

NH3_emssn_PAF1_coal_hrly = 2.39E-04 lb/unit-hr This value, listed in cell PAF1!G30, is based on CY05-average NH3 emssn factr & Title V max heat-input capacity.

Equation (4):

NH4_salt_stk_emssn_PAF1_coal = (NH4_salt_stk_emssn_PAF1_2_ILB+NH4_salt_stk_emssn_PAF1_2_PRB)*coal_burn_PAF1_ILB_SCR/coal_burn_PAF1_2_ILB_SCR*(ton/2000 lb)

NH4_salt_stk_emssn_PAF1_coal = 2.61E-01 tpy Ammonium (NH4)-salt stack emissions are subsumed within total PM emissions & are not separately reported.

PAF Plant-Total Fugitive-Air NH3 Emission Estimates:

Equation (1):

SCR_NH3_fugitive_emssn_PAF = SCR_NH3_fugitive_emssn_PAF1_2_ILB+SCR_NH3_fugitive_emssn_PAF1_2_PRB+SCR_NH3_fugitive_emssn_PAF3_ILB+SCR_NH3_fugitive_emssn_PAF3_PRB

SCR_NH3_fugitive_emssn_PAF = 1.07E+04 lb/yr

Equation (2):

Unloading_NH3_fugitive_emssn_PAF = anhydrous_NH3_recpts_truck*unloading_emssn_factr_truck_NH3+anhydrous_NH3_recpts_rail*unloading_emssn_factr_rail

Unloading_NH3_fugitive_emssn_PAF = 1.56E+01 lb/yr

Equation (3):

BWT_NH3_fugitive_emssn_PAF = aqueous_NH3_rcpts*aqueous_NH3_wt_fractn/100*BWT_pond_NH3_air

BWT_NH3_fugitive_emssn_PAF = 1.56E+03 lb/yr

Equation (4):

NH3_fugitive_emssn_PAF = (SCR_NH3_fugitive_emssn_PAF+Unloading_NH3_fugitive_emssn_PAF+BWT_NH3_fugitive_emssn_PAF)*(ton/2000 lb)

NH3_fugitive_emssn_PAF = 6.14E+00 tpy CY05 PAF plant-total NH3 fugitive air emissions, listed in cell W22 of "air" worksheet

PAF Unit 1 Routine Coal-fired Trace-Element Hazardous-Air-Pollutant (HAP) Emission Estimates:

Trace-element emission estimates were derived from EPRI's Emission Factor Handbook (EFH). Lead (Pb) is typical of PM trace elements; hydrogen chloride (HCl) and mercury (Hg) are examples of

gaseous trace-element HAP with significantly different emission-estimation methodologies.

Pb Emission Estimates:

PAF Unit 1 Illinois Basin (ILB) coal:

Equation (1):

Pb_emssn_factr_PAF1_ILB = 3.4*(Pb_in_ILB_mass*(1-coal_H2O_PAF_ILB/100)*(100/coal_ash_PAF_ILB)*PM_fil_emssn_factr_PAF1_coal)^0.80

Pb_emssn_factr_PAF1_ILB = 2.18E+01 lb/10^12 Btu (TBtu) = EFH Median Pb Emission Correlation Estimate 10

Page 6 of 12
calcs

Equation (2):

Pb_in_ILB_energy = Pb_in_ILB_mass*(kg/10^6 mg)/coal_heat_PAF_ILB*(1-coal_H2O_PAF_ILB/100)*(10^12 Btu/TBtu)

Pb_in_ILB_energy = 1.07E+03 lb/TBtu

Equation (3):

Pb_contrl_effncy_PAF1_ILB = (1-Pb_emssn_factr_PAF1_ILB/Pb_in_ILB_energy)*100%

Pb_contrl_effncy_PAF1_ILB = 97.96 % = PAF Unit 1 Boiler/FGD contrl effncy for Pb in ILB coal 

Equation (4):

Pb_emssn_PAF1_ILB = Pb_emssn_factr_PAF1_ILB*heat_input_PAF1_ILB*(ton/2000 lb)

Pb_emssn_PAF1_ILB = 4.63E-01 tpy This value is listed in cell F41 of "PAF1_ILB" worksheet (PAF1_ILB!F41).

PAF Unit 1 Powder River Basin (PRB) subbituminous coal:

Equation (5):

Pb_emssn_factr_PAF1_PRB = 3.4*(Pb_in_PRB_mass*(1-coal_H2O_PAF_PRB/100)*(100/coal_ash_PAF_PRB)*PM_fil_emssn_factr_PAF1_coal)^0.80

Pb_emssn_factr_PAF1_PRB = 8.45E+00 lb/TBtu = EFH Median Pb Emission Correlation Estimate 10

Equation (6):

Pb_in_PRB_energy = Pb_in_PRB_mass*(kg/10^6 mg)/coal_heat_PAF_PRB*(1-coal_H2O_PAF_PRB/100)*(10^12 Btu/TBtu)

Pb_in_PRB_energy = 2.64E+02 lb/TBtu

Equation (7):

Pb_contrl_effncy_PAF1_PRB = (1-Pb_emssn_factr_PAF1_PRB/Pb_in_PRB_energy)*100%

Pb_contrl_effncy_PAF1_PRB = 96.81 % = PAF Unit 1 Boiler/FGD contrl effncy for Pb in PRB coal 

Equation (8):

Pb_emssn_PAF1_PRB = Pb_emssn_factr_PAF1_PRB*heat_input_PAF1_PRB*(ton/2000 lb)

Pb_emssn_PAF1_PRB = 1.38E-03 tpy This value is listed in cell F41 of "PAF1_PRB" worksheet (PAF1_PRB!F41).

PAF Unit 1 total-coal Pb emssn:

Equation (9):

Pb_emssn_PAF1_coal = Pb_emssn_PAF1_ILB+Pb_emssn_PAF1_PRB

Pb_emssn_PAF1_coal = 4.64E-01 tpy This value is listed in cell PAF1!F41 and is included in cell B35 of "air" worksheet.

Equation (10):

Pb_in_coal_energy_PAF1 = (Pb_in_ILB_energy*heat_input_PAF1_ILB+Pb_in_PRB_energy*heat_input_PAF1_PRB)/heat_input_PAF1_coal

Pb_in_coal_energy_PAF1 = 1.06E+03 lb/TBtu

Equation (11):

Pb_emssn_factr_PAF1_coal = Pb_emssn_PAF1_coal*(2000 lb/ton)/heat_input_PAF1_coal

Pb_emssn_factr_PAF1_coal = 2.17E+01 lb/TBtu

Equation (12):

Pb_emssn_PAF1_coal_hrly = max_heat_input_PAF1*Pb_emssn_factr_PAF1_coal*(TBtu/10^6 MBtu)

Pb_emssn_PAF1_coal_hrly = 1.51E-01 lb/unit-hr This value, listed in cell PAF1!G41, is based on average Pb emssn factr & Title V max heat-input capacity.

Equation (13):

Pb_contrl_effncy_PAF1 = (1-Pb_emssn_factr_PAF1_coal/Pb_in_coal_energy_PAF1)*100

Pb_contrl_effncy_PAF1 = 97.96 % PAF Unit 1 coal-region weighted-avg. boiler/FGD Pb contrl effncy (cell E41 in "PAF1" wksheet)

Note that coal-region weighted-avg. boiler/FGD coal trace-element control efficiencies (e.g., cell E41 in "PAF1" wksheet for Pb) were used to estimate alternate-fuel contol efficiencies.

HCl Emission Estimates:

PAF Unit 1 Illinois Basin (ILB) bituminous coal:

Equation (1):

Cl_in_ILB_energy = Cl_in_ILB_mass*(kg/10^6 mg)/coal_heat_PAF_ILB*(10^12 Btu/TBtu)

Cl_in_ILB_energy = 5.23E+04 lb Cl/TBtu

Equation (2):

HCl_emssn_factr_PAF1_ILB = Cl_in_ILB_energy*(1-Cl_contrl_effncy_FGD/100)*HCl_mol_wt/Cl_mol_wt

HCl_emssn_factr_PAF1_ILB = 1.62E+03 lb HCl/TBtu = EFH Recommended HCl Emission Factor Estimate 10

Equation (3):

HCl_emssn_PAF1_ILB = HCl_emssn_factr_PAF1_ILB*heat_input_PAF1_ILB*(ton/2000 lb)

HCl_emssn_PAF1_ILB = 3.43E+01 tpy This value is listed in cell F52 of "PAF1_ILB" worksheet (PAF1_ILB!F52).

PAF Unit 1 Powder River Basin (PRB) subbituminous coal:

Equation (4):

Cl_in_PRB_energy = Cl_in_PRB_mass*(kg/10^6 mg)/coal_heat_PAF_PRB*(10^12 Btu/TBtu)

Cl_in_PRB_energy = 5.70E+03 lb Cl/TBtu

Equation (5):

HCl_emssn_factr_PAF1_PRB = Cl_in_PRB_energy*(1-Cl_contrl_effncy_FGD/100)*HCl_mol_wt/Cl_mol_wt

HCl_emssn_factr_PAF1_PRB = 1.76E+02 lb HCl/TBtu = EFH Recommended HCl Emission Factor Estimate 10

Equation (6):

HCl_emssn_PAF1_PRB = HCl_emssn_factr_PAF1_PRB*heat_input_PAF1_PRB*(ton/2000 lb)

HCl_emssn_PAF1_PRB = 2.87E-02 tpy This value is listed in cell PAF1_PRB!F52.

PAF Unit 1 total-coal HCl emssn:

Equation (7):

HCl_emssn_PAF1_coal = HCl_emssn_PAF1_ILB+HCl_emssn_PAF1_PRB

HCl_emssn_PAF1_coal = 3.44E+01 tpy This value is listed in cell PAF1!F52 and is included in air!B30.

Equation (8):

Cl_in_coal_energy_PAF = (Cl_in_ILB_energy*heat_input_PAF1_ILB+Cl_in_PRB_energy*heat_input_PAF1_PRB)/heat_input_PAF1_coal

Cl_in_coal_energy_PAF = 5.20E+04 lb/TBtu

Equation (9):

HCl_emssn_factr_uncontrolld_PAF_coal = Cl_in_coal_energy_PAF*HCl_mol_wt/Cl_mol_wt

HCl_emssn_factr_uncontrolld_PAF_coal = 5.35E+04 lb/TBtu

Equation (10):

HCl_emssn_factr_PAF1_coal = HCl_emssn_PAF1_coal*(2000 lb/ton)/heat_input_PAF1_coal

HCl_emssn_factr_PAF1_coal = 1.60E+03 lb/TBtu

Equation (11):

HCl_emssn_PAF1_coal_hrly = max_heat_input_PAF1*HCl_emssn_factr_PAF1_coal*(TBtu/10^6 MBtu)

HCl_emssn_PAF1_coal_hrly = 1.12E+01 lb/unit-hr This value, listed in cell PAF1!G52, is based on average HCl emssn factr & Title V max heat-input capacity.

Equation (12):

HCl_contrl_effncy_PAF1_coal = (1-HCl_emssn_factr_PAF1_coal/HCl_emssn_factr_uncontrolld_PAF_coal)*100

HCl_contrl_effncy_PAF1_coal = 97.00 % PAF Unit 1 coal-region weighted-avg. boiler/FGD total-coal HCl control efficiency

Page 7 of 12
calcs

Hg Emission Estimates:

PAF Unit 1 Illinois Basin (ILB) bituminous coal:

Equation (1):

Hg_in_ILB_energy = Hg_in_ILB_mass*(kg/10^6 mg)/coal_heat_PAF_ILB*(1-coal_H2O_PAF_ILB/100)*(10^12 Btu/TBtu)

Hg_in_ILB_energy = 6.11E+00 lb/TBtu

Equation (2):

Hg_contrl_effncy_PAF1_ILB_SCR = Hg_removal_effncy_SCR_FGDW_bitum

Hg_contrl_effncy_PAF1_ILB_SCR = 86 % Hg removal efficiency for Eastern-bitum-fired boilers w/selective-catalytic-reduction (SCR) reactor & FGD scrubber 10

Equation (3):

Hg_contrl_effncy_PAF1_ILB_SCR_bypass = (Hg_removal_multiplier_FGDW*ln(Cl_in_coal_ILB/(1-coal_H2O_PAF_ILB/100))+Hg_removal_constant_FGDW)*100%

Hg_contrl_effncy_PAF1_ILB_SCR_bypass = 18.69 % EFH Boiler/FGD contrl effncy for Hg in ILB coal (when flue-gas path bypasses SCR reactor) 10

Equation (4):

Hg_contrl_effncy_PAF1_ILB = Hg_contrl_effncy_PAF1_ILB_SCR*SCR_oper_factr_PAF1+Hg_contrl_effncy_PAF1_ILB_SCR_bypass*(1-SCR_oper_factr_PAF1)

Hg_contrl_effncy_PAF1_ILB = 51.32 %

Equation (5):

Hg_emssn_factr_PAF1_ILB = Hg_in_ILB_energy*(1-Hg_contrl_effncy_PAF1_ILB/100)

Hg_emssn_factr_PAF1_ILB = 2.97E+00 lb/TBtu

Equation (6):

Hg_emssn_PAF1_ILB = Hg_emssn_factr_PAF1_ILB*heat_input_PAF1_ILB*(ton/2000 lb)

Hg_emssn_PAF1_ILB = 6.32E-02 tpy This value is listed in cell F54 of "PAF1_ILB" worksheet (PAF1_ILB!F54).

PAF Unit 1 Powder River Basin (PRB) subbituminous coal:

Equation (7):

Hg_in_PRB_energy = Hg_in_PRB_mass*(kg/10^6 mg)/coal_heat_PAF_PRB*(1-coal_H2O_PAF_PRB/100)*(10^12 Btu/TBtu)

Hg_in_PRB_energy = 4.96E+00 lb/TBtu

Equation (8):

Hg_contrl_effncy_PAF1_PRB = (Hg_removal_multiplier_FGDW*ln(Cl_in_coal_PRB/(1-coal_H2O_PAF_PRB/100))+Hg_removal_constant_FGDW)*100%

Hg_contrl_effncy_PAF1_PRB = 5.32 % EFH Boiler/FGD contrl effncy for Hg in PRB coal (negligible SCR effects on Hg control when burning subbitum coal) 10

Equation (9):

Hg_emssn_factr_PAF1_PRB = Hg_in_PRB_energy*(1-Hg_contrl_effncy_PAF1_PRB/100)

Hg_emssn_factr_PAF1_PRB = 4.69E+00 lb/TBtu

Equation (10):

Hg_emssn_PAF1_PRB = Hg_emssn_factr_PAF1_PRB*heat_input_PAF1_PRB*(ton/2000 lb)

Hg_emssn_PAF1_PRB = 7.65E-04 tpy This value is listed in cell PAF1_PRB!F54.

PAF Unit 1 total-coal Hg emssn:

Equation (11):

Hg_emssn_PAF1_coal = Hg_emssn_PAF1_ILB+Hg_emssn_PAF1_PRB

Hg_emssn_PAF1_coal = 6.39E-02 tpy This value is listed in cell PAF1!F54 and is included in air!B37.

Equation (12):

Hg_in_coal_energy_PAF = (Hg_in_ILB_energy*heat_input_PAF1_ILB+Hg_in_PRB_energy*heat_input_PAF1_PRB)/heat_input_PAF1_coal

Hg_in_coal_energy_PAF = 6.10E+00 lb/TBtu

Equation (13):

Hg_emssn_factr_PAF1_coal = Hg_emssn_PAF1_coal*(2000 lb/ton)/heat_input_PAF1_coal

Hg_emssn_factr_PAF1_coal = 2.99E+00 lb/TBtu

Equation (14):

Hg_emssn_PAF1_coal_hrly = max_heat_input_PAF1*Hg_emssn_factr_PAF1_coal*(TBtu/10^6 MBtu)

Hg_emssn_PAF1_coal_hrly = 2.08E-02 lb/unit-hr This value, listed in cell PAF1!G54, is based on average Hg emssn factr & Title V max heat-input capacity.

Equation (15):

Hg_contrl_effncy_PAF1_coal = (1-Hg_emssn_factr_PAF1_coal/Hg_in_coal_energy_PAF)*100

Hg_contrl_effncy_PAF1_coal = 51.0 % PAF Unit 1 coal-region weighted-avg. boiler/SCR/FGD total-coal Hg control efficiency

PAF Unit 1 Routine Coal-fired Organic HAP Emission Estimates:

Biphenyl (CAS No. 92524) coal-fired emission estimates based on EPRI's Emission Factor Handbook (EFH) are typical for organic HAP.

Biphenyl_emssn_factr_coal = 0.16 lb/TBtu EFH Log-normal-mean biphenyl coal-fired emission factor 10

Equation (1):

Biphenyl_emssn_PAF1_coal = Biphenyl_emssn_factr_coal*heat_input_PAF1_coal*(ton/2000lb)

Biphenyl_emssn_PAF1_coal = 3.43E-03 tpy = PAF Unit 1 biphenyl emission estimate, listed in cell PAF1!F73 and included in air!B67.

PAF Unit 1 Routine Coal-fired Radionuclide Emission Estimates:

Radionuclides_in_fly_ash = 53.1 pCi/g of emitted PM =sum EFH geom mean factrs for Pb-210, Po-210, Ra-226, 10

Ra-228, Th-228, Th-230, Th-232, U-234, U-235, & U-238

Equation (1):

Radionuclide_emssn_factr_PAF1_coal = Radionuclides_in_fly_ash*PM_fil_emssn_factr_PAF1_coal*(453.5924 g/lb)

Radionuclide_emssn_factr_PAF1_coal = 1.72E+03 pCi/MBtu

Equation (2):

Radionuclide_emssn_PAF1_coal = Radionuclide_emssn_factr_PAF1_coal*(10^6 MBtu/TBtu)*heat_input_PAF1_coal*(1 Ci/10^12 pCi)

Radionuclide_emssn_PAF1_coal = 7.35E-02 Ci/yr This value is given in PAF1!F159 and is included in air!B161.

Sample Calculations for PAF Unit 1 Alternate-Fuel (Lightoff-Oil) Criteria-Pollutant & Hazardous-Air-Pollutant (HAP) Emission Estimates

Distillate fuel oil is fired for lightoff during unit startup (and may also be fired at other times to ensure flame stability). During the oil-fired portion of startups for PAF Unit 3, the electrostatic-precipitator (ESP) PM control

system is not energized due to safety concerns. PAF Units 1-2 FGD scrubbers are in-service whenever fire is in the boiler. PAF lightoff-oil emissions were conservatively estimated using AP-42 uncontrolled emission

factors (Ref. 21) for distillate fuel oil combustion.

General Input Variables: Value Units Notes Reference

lightoff_oil_burn_PAF1_2 = 179,956 gal/yr CY05 PAF Units 1-2 distillate (No. 2) fuel-oil burn. 2

turbine_startups_PAF1 = 12 Number of CY05 PAF Unit 1 turbine startups 2

turbine_startups_PAF1_2 = 16 Number of CY05 PAF Units 1-2 total turbine startups 2

lightoff_oil_heat_PAF = 138,500 Btu/gal CY05 PAF plant-total lightoff-oil heat content (HHV) 2

lightoff_oil_S_PAF = 0.2 % weight CY05 PAF plant-total lightoff-oil sulfur content 2

PM_fil_emssn_factr_distillate_oil = 2 lb/10^3 gal (kgal) Filterable particulate-matter (PM_fil) uncontrolled emissn factr for distillate-oil combustn in boilers 21

SO2_emssn_factr_distillate_oil = 142 lb/(kgal-%S) Sulfur dioxide (SO2) uncontrolled emissn factr for distillate-oil combustion in boilers 21

NOx_emssn_factr_distillate_oil = 24 lb/kgal Nitrogen oxides (NOx) uncontrolled emissn factr for distillate-oil combustion in boilers 21

CO_emssn_factr_distillate_oil = 5 lb/kgal Carbon monoxide (CO) uncontrolled emissn factr for distillate-oil combustion in boilers 21

VOC_emssn_factr_distillate_oil = 0.2 lb/kgal Volatile organic compds (VOC) uncontrolled emissn factr for distillate-oil combustion in boilers 21

SO3_emssn_factr_distillate_oil = 5.7 lb/(kgal-%S) Sulfur trioxide (SO3) uncontrolled emissn factr for distillate-oil combustion in boilers 21

SO3_mol_wt = 80.0622 lb/lb-mole Sulfur trioxide (SO3) molecular weight 11

Page 8 of 12
calcs

Trace-Element & Organic HAP Inputs:

Pb_emssn_factr_distillate_oil = 9 lb/10^12 Btu (TBtu) Lead (Pb) emissn factr for distillate-oil combustion in boilers 21

CH2O_emssn_factr_distillate_oil = 0.061 lb/kgal Formaldehyde (CH2O) uncontrolled emission factr for distillate-oil combustion in boilers 21

PAF Unit 1 Lightoff-Oil Criteria-Pollutant & Non-HAP Emission Estimates:

Filterable Particulate Matter (PM_fil)

Equation (1):

lightoff_oil_burn_PAF1 = lightoff_oil_burn_PAF*turbine_startups_PAF1/turbine_startups_PAF

lightoff_oil_burn_PAF1 = 134,967 gal/yr

Equation (2):

PM_fil_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*PM_fil_emssn_factr_distillate_oil*(ton/2000 lb)

PM_fil_emssn_PAF1_lightoff_oil = 1.35E-01 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C13.

Sulfur Dioxide (SO2)

Equation (3):

SO2_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*SO2_emssn_factr_distillate_oil*lightoff_oil_S_PAF*(ton/2000 lb)

SO2_emssn_PAF1_lightoff_oil = 1.92E+00 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C17.

Nitrogen Oxides (NOx)

Equation (4):

NOx_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*NOx_emssn_factr_distillate_oil*(ton/2000 lb)

NOx_emssn_PAF1_lightoff_oil = 1.62E+00 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C18.

Carbon Monoxide (CO)

Equation (5):

CO_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*CO_emssn_factr_distillate_oil*(ton/2000 lb)

CO_emssn_PAF1_lightoff_oil = 3.37E-01 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C19.

Volatile Organic Compounds (VOC)

Equation (6):

VOC_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*VOC_emssn_factr_distillate_oil*(ton/2000 lb)

VOC_emssn_PAF1_lightoff_oil = 1.35E-02 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C20.

Sulfuric Acid (H2SO4)

Equation (7):

H2SO4_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*SO3_emssn_factr_distillate_oil*lightoff_oil_S_PAF*H2SO4_to_SO3_molar_ratio/100*H2SO4_mol_wt/SO3_mol_wt*(ton/2000 lb)

H2SO4_emssn_PAF1_lightoff_oil = 9.42E-02 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C21.

PAF Unit 1 Lightoff-Oil Hazardous-Air-Pollutant (HAP) Emission Estimates:

Lead (Pb) and formaldehyde (CH2O) emission estimates based on EPA's AP-42 distillate-oil emission factors are typical for lightoff-oil trace-element and organic HAP emissions, respectively.

Pb Emission Estimates:

Equation (1):

Pb_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*lightoff_oil_heat_PAF*Pb_emssn_factr_distillate_oil*(TBtu/10^12 Btu)*(ton/2000 lb)

Pb_emssn_PAF1_lightoff_oil = 8.41E-05 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C35.

Formaldehyde (CH2O) Emission Estimates:

Equation (2):

CH2O_emssn_PAF1_lightoff_oil = lightoff_oil_burn_PAF1*(kgal/10^3 gal)*CH2O_emssn_factr_distillate_oil*(ton/2000 lb)

CH2O_emssn_PAF1_lightoff_oil = 4.12E-03 tpy This value is listed in Table 11 of the "alt_fuel" wksheet & is included in air!C80.

Sample Calculations for PAF Unit 1 Alternate-Fuel (Used-Oil) Criteria-Pollutant & Hazardous-Air-Pollutant (HAP) Emission Estimates

General Input Variables: Value Units Notes Reference

used_oil_burn_PAF1 = 16,335 gallons/yr (gal/yr) CY05 PAF Unit 1 used-oil burn 22

specific_grav = 0.9 g/mL Nominal value for TVA-wide used-oil samples 23

used_oil_ash = 0.1 weight % Nominal value for TVA-wide used-oil samples

used_oil_S 0.4 weight % Nominal value for TVA-wide used-oil samples

PM_fil_emssn_factr_used_oil = 64 lb/(kgal-%ash) Filterable particulate-matter (PM_fil) uncontrolled emissn factr for used-oil combustn in boilers 24

PM10_fil_emssn_factr_used_oil = 51 lb/(kgal-%ash) Filterable particulate-matter (PM_fil) uncontrolled emissn factr for used-oil combustn in boilers 24

SO2_emssn_factr_used_oil = 147 lb/(kgal-%S) Sulfur dioxide (SO2) uncontrolled emissn factr for used-oil combustion in boilers 24

NOx_emssn_factr_used_oil = 19 lb/kgal Nitrogen oxides (NOx) uncontrolled emissn factr for used-oil combustion in boilers 24

CO_emssn_factr_used_oil = 5 lb/kgal Carbon monoxide (CO) uncontrolled emissn factr for used-oil combustion in boilers 24

VOC_emssn_factr_used_oil = 1 lb/kgal Volatile organic compds (VOC) uncontrolled emissn factr for used-oil combustion in boilers 24

PM_fil_emssn_factr_PAF1_coal = 0.071 lb/10^6 Btu (MBtu) CY05 PAF Unit 1 coal-fired filterable particulate-matter (PM_fil) stack-test measurements (average) 4

SOx_uncontrlld_emssn_factr_bitum = 38 lb/(ton as-fired coal*%S) AP-42 uncontrolled bituminous-coal SOx emssion factor (expressed as SO2) for cyclone-fired boilers 6

SOx_uncontrlld_emssn_factr_subbit = 35 lb/(ton as-fired coal*%S) AP-42 uncontrolled subbituminous-coal SOx emssion factor (expressed as SO2) for cyclone-fired boilers 6

NOx_uncontrlld_emssn_factr_bitum = 33 lb/(ton AR coal) AP-42 uncontrolled bituminous-coal NOx emission factor for cyclone-fired boilers 6

NOx_uncontrlld_emssn_factr_subbit = 17 lb/(ton AR coal) AP-42 uncontrolled subbituminous-coal NOx emission factor for cyclone-fired boilers 6

SO2_emssn_PAF1_CEMS = 13,563 tons/yr (tpy) CY05 PAF Unit 1 CEMS sulfur dioxide (SO2) emssn data (coal + alternate fuels) 7

heat_input_PAF1_CEMS = 43,191,735 x 10^6 Btu/yr (MBtu/yr) CY05 PAF Unit 1 CEMS heat-input estimate (coal + alternate fuels) 7

NOx_emssn_PAF1_CEMS = 11,466 tpy CY05 PAF Unit 1 CEMS nitrogen oxides (NOx) emission measurements (coal + alternate fuels) 7

CO_contrl_effncy_PAF1 = 0 % PAF boilers have no add-on CO control equipment 

VOC_contrl_effncy_PAF1 = 0 % PAF boilers have no add-on VOC control equipment 

Trace-Element HAP Inputs, taking Lead (Pb) & Hydrogen Chloride (HCl) as examples:

Pb_in_used_oil_mass = 2.42 mg/kg (as-fired) Mean lead (Pb) mass concentration in CY03 PAF used-oil analyses 25

Cl_in_used_oil_mass = 179 mg/kg (as-fired) Mean total halogen (presume Cl) mass concentration in CY03 PAF used-oil analyses 25

HCl_emssn_factr_used_oil = 66 lb/(kgal-%Cl) Hydrogen chloride (HCl) uncontrolled emissn factr for used-oil combustion in boilers 24

Pb_contrl_effncy_PAF1 = 97.96 % PAF Unit 1 coal-region weighted-avg. boiler/FGD Pb contrl effncy (cell E40 in "PAF1" wksheet)

HCl_contrl_effncy_PAF1 = 97.00 % PAF Unit 1 coal-region weighted-avg. boiler/FGD total-coal HCl control efficiency (cell E51 in "PAF1" wksheet)

PAF Unit 1 Used-Oil Criteria-Pollutant Emission Estimates:

Filterable Particulate Matter (PM_fil)

Equation (1):

PM_fil_inputs_PAF1_used_oil = used_oil_burn_PAF1*PM_fil_emssn_factr_used_oil*(kgal/1000 gal)*used_oil_ash*(ton/2000 lb)

PM_fil_inputs_PAF1_used_oil = 5.23E-02 tpy

Equation (2):

coal_ash_PAF1 = (coal_burn_PAF1_ILB*coal_ash_PAF_ILB+coal_burn_PAF1_PRB*coal_ash_PAF_PRB)/coal_burn_PAF1

coal_ash_PAF1 = 8.57 %-weight (AR basis)

Equation (3):

coal_heat_PAF1 = (coal_burn_PAF1_ILB*coal_heat_PAF_ILB+coal_burn_PAF1_PRB*coal_heat_PAF_PRB)/coal_burn_PAF1

coal_heat_PAF1 = 1.15E+04 Btu [HHV]/lb AR basis

Page 9 of 12
calcs

Equation (4):

PM_fil_uncontrlld_emssn_factr_PAF1_coal = (coal_ash_PAF1/100)/coal_heat_PAF1*(ash_partition_to_flue_gas_PAF/100)*(10^6 Btu/MBtu)

PM_fil_uncontrlld_emssn_factr_PAF1_coal = 1.87E+00 lb/MBtu

Equation (5):

PM_fil_contrl_effncy_PAF1 = (1-PM_fil_emssn_factr_PAF1_coal/PM_fil_uncontrlld_emssn_factr_PAF1_coal)*100

PM_fil_contrl_effncy_PAF1 = 96.2 %

Equation (6):

PM_fil_emssn_PAF1_used_oil = PM_fil_inputs_PAF1_used_oil*(1-PM_fil_contrl_effncy_PAF1/100)

PM_fil_emssn_PAF1_used_oil = 1.99E-03 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!$C$13.

Sulfur Dioxide (SO2)

Equation (7):

coal_S_PAF1 = (coal_burn_PAF1_ILB*coal_S_PAF_ILB+coal_burn_PAF1_PRB*coal_S_PAF_PRB)/coal_burn_PAF1

coal_S_PAF1 = 2.67 %-weight (AR basis)

Equation (8):

SO2_uncontrlld_emssn_factr_PAF1_coal = (SOx_uncontrlld_emssn_factr_bitum*coal_S_PAF1_ILB*coal_burn_PAF1_ILB+

SOx_uncontrlld_emssn_factr_subbit*coal_S_PAF1_PRB*coal_burn_PAF1_PRB)/(coal_heat_PAF1*coal_burn_PAF1*2000 lb/ton)*(10^6 Btu/MBtu)

SO2_uncontrlld_emssn_factr_PAF1_coal = 4.42E+00 lb/MBtu

Equation (9):

SO2_emssn_factr_PAF1_CEMS = SO2_emssn_PAF1_CEMS*(2000 lb/ton)/heat_input_PAF1_CEMS

SO2_emssn_factr_PAF1_CEMS = 6.28E-01 lb/MBtu

Equation (10):

SO2_contrl_effncy_PAF1 = (1-SO2_emssn_factr_PAF1_CEMS/SO2_uncontrlld_emssn_factr_PAF1_coal)*100

SO2_contrl_effncy_PAF1 = 85.78 %

Equation (11):

SO2_emssn_PAF1_used_oil = used_oil_burn_PAF1*SO2_emssn_factr_used_oil*(kgal/1000 gal)*used_oil_S*(1-SO2_contrl_effncy_PAF1/100)*(ton/2000 lb)

SO2_emssn_PAF1_used_oil = 6.83E-02 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!$C$17.

Nitrogen Oxides (NOx)

Equation (12):

NOx_uncontrlld_emssn_factr_PAF1_coal = (NOx_uncontrlld_emssn_factr_bitum*coal_burn_PAF1_ILB+NOx_uncontrlld_emssn_factr_subbit*coal_burn_PAF1_PRB)/(coal_heat_PAF1*coal_burn_PAF1*2000 lb/ton)*(10^6 Btu/MBtu)

NOx_uncontrlld_emssn_factr_PAF1_coal = 1.43E+00 lb/MBtu

Equation (13):

NOx_emssn_factr_PAF1_CEMS = NOx_emssn_PAF1_CEMS*(2000 lb/ton)/heat_input_PAF1_CEMS

NOx_emssn_factr_PAF1_CEMS = 5.31E-01 lb/MBtu

Equation (14):

NOx_contrl_effncy_PAF1 = (1-NOx_emssn_factr_PAF1_CEMS/NOx_uncontrlld_emssn_factr_PAF1_coal)*100

NOx_contrl_effncy_PAF1 = 62.91 %

Equation (15):

NOx_emssn_PAF1_used_oil = used_oil_burn_PAF1*NOx_emssn_factr_used_oil*(kgal/1000 gal)*(1-NOx_contrl_effncy_PAF1/100)*(ton/2000 lb)

NOx_emssn_PAF1_used_oil = 5.76E-02 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!$C$18.

Carbon Monoxide (CO)

Equation (16):

CO_emssn_PAF1_used_oil = used_oil_burn_PAF1*CO_emssn_factr_used_oil*(kgal/1000 gal)*(1-CO_contrl_effncy_PAF1/100)*(ton/2000 lb)

CO_emssn_PAF1_used_oil = 4.08E-02 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!$C$19.

Volatile Organic Compounds (VOC)

Equation (17):

VOC_emssn_PAF1_used_oil = used_oil_burn_PAF1*VOC_emssn_factr_used_oil*(kgal/1000 gal)*(1-VOC_contrl_effncy_PAF1/100)*(ton/2000 lb)

VOC_emssn_PAF1_used_oil = 8.17E-03 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!$C$20.

PAF Unit 1 Used-Oil Trace-Element Hazardous-Air-Pollutant (HAP) Emission Estimates:

Lead (Pb) and Hydrogen Chloride (HCl) emission estimates based on CY03 analyses & AP-42 emission factors are typical for used-oil trace-element HAP emissions.

Pb Emission Estimates:

Equation (1):

Pb_inputs_PAF1_used_oil = used_oil_burn_PAF1*specific_grav*(3785.412 mL/gal)*(lb/453.5924g)*Pb_in_used_oil_mass*(1kg/10^6mg)*(ton/2000 lb)

Pb_inputs_PAF1_used_oil = 1.49E-04 tpy

Equation (2):

Pb_emssn_PAF1_used_oil = Pb_inputs_PAF1_used_oil*(1-Pb_contrl_effncy_PAF1/100)

Pb_emssn_PAF1_used_oil = 3.0E-06 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!C35.

HCl Emission Estimates:

Equation (3):

HCl_emssn_PAF1_used_oil = used_oil_burn_PAF1*HCl_emssn_factr_used_oil*(kgal/1000 gal)*Cl_in_used_oil_mass*(kg/10^6 mg)*(100%)*(1-HCl_contrl_effncy_PAF1/100)*(ton/2000 lb)

HCl_emssn_PAF1_used_oil = 2.9E-04 tpy This value is listed in Table 4 of the "alt_fuel" wksheet & is included in air!$C$30.

Sample Calculations for PAF Unit 1 Alternate-Fuel (Tire-Derived-Fuel [TDF]) Criteria-Pollutant & Hazardous-Air-Pollutant (HAP) Emission Estimates

General Input Variables: Value Units Notes Reference

TDF_burn_PAF = 0 tons/yr (tpy) CY05 PAF plant-total as received/fired (AR) tire-derived-fuel (TDF) burn 26

TDF_heat_ALF = 16,363 Btu/lb CY03 Allen Fossil Plant (ALF) TDF AR heat content 26

TDF_ash_ALF = 6.26 % weight CY03 ALF TDF AR ash content 26

SOx_uncontrlld_emssn_factr_ALF_TDF = 1.86 lb SO2/10^6 Btu CY03 ALF TDF sulfur-oxides (SOx) emission factor (expressed as sulfur dioxide [SO2]) 26

PM & Gaseous Trace-Element HAP Inputs:

Pb_uncontrlld_emssn_factr_TDF = 3.86E-04 lb/10^6 Btu (MBtu) TDF uncontrolled lead (Pb) emission factor 27

Pb_contrl_effncy_PAF1 = 97.96 % PAF Unit 1 coal-region weighted-avg. boiler/FGD Pb contrl effncy (cell E40 in "PAF1" wksheet)

PAF Unit 1 TDF-fired Criteria-Pollutant Emission Estimates:

Filterable Particulate Matter (PM_fil)

Equation (1):

TDF_burn_PAF1 = TDF_burn_PAF*coal_burn_PAF1/coal_burn_PAF

TDF_burn_PAF1 = 0.00E+00 tpy CY05 PAF plant-total TDF burn apportioned according to unit-specific share of plant-total coal burn.

Equation (2):

PM_fil_uncontrlld_emssn_factr_PAF1_TDF = (TDF_ash_ALF/100)/TDF_heat_ALF*(ash_partition_to_flue_gas_PAF/100)*(10^6 Btu/MBtu)

PM_fil_uncontrlld_emssn_factr_PAF1_TDF = 9.56E-01 lb/MBtu

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calcs

Equation (3):

PM_fil_emssn_PAF1_TDF = TDF_burn_PAF1*(2000 lb/ton)*TDF_heat_ALF*PM_fil_uncontrlld_emssn_factr_PAF1_TDF*(MBtu/10^6 Btu)*(1-PM_fil_contrl_effncy_PAF1/100)*(ton/2000 lb)

PM_fil_emssn_PAF1_TDF = 0.00E+00 tpy This value is listed in Table 8 of the "alt_fuel" wksheet & is included in air!C13.

Sulfur Dioxide (SO2)

Equation (4):

heat_input_PAF1_TDF = TDF_burn_PAF1*(2000 lb/ton)*TDF_heat_ALF*(MBtu/10^6 Btu)

heat_input_PAF1_TDF = 0.00E+00 MBtu/yr

Equation (5):

SO2_emssn_PAF1_TDF = heat_input_PAF1_TDF*SOx_uncontrlld_emssn_factr_ALF_TDF*(1-SO2_contrl_effncy_PAF1/100)*(ton/2000 lb)

SO2_emssn_PAF1_TDF = 0.00E+00 tpy This value is listed in Table 8 of the "alt_fuel" wksheet & is included in air!C17.

PAF Unit 1 TDF-fired Trace-Element Hazardous-Air-Pollutant (HAP) Emission Estimates:

Lead (Pb) emission estimates based on EPA's TDF emission factor are typical for TDF trace-element HAP emissions.

Pb Emission Estimates:

Equation (1):

Pb_emssn_PAF1_TDF = heat_input_PAF1_TDF*Pb_uncontrlld_emssn_factr_TDF*(1-Pb_contrl_effncy_PAF1/100)*(ton/2000 lb)

Pb_emssn_PAF1_TDF = 0.00E+00 tpy This value is listed in Table 8 of the "alt_fuel" wksheet & is included in air!C35.

Sample Calculations for PAF Unit 1 Alternate-Fuel (Wood-Residue) Criteria-Pollutant & Hazardous-Air-Pollutant (HAP) Emission Estimates

General Input Variables: Value Units Notes Reference

WW_burn_PAF = 0 tons/yr (tpy) CY05 PAF plant-total woodwaste (WW) burn 26

WW_H2O_COF = 45.66 % CY03 Colbert Fossil Plant (COF) WW moisture content 26

WW_ash_COF = 5.66 % (as-received) CY03 COF WW as-received (AR) ash content 26

WW_S_COF = 0.06 % (as-received) CY03 COF WW AR sulfur content 26

WW_heat_COF = 4,372 Btu/lb (as-received) CY03 COF WW AR heat content 26

PM_fil_emssn_factr_WW_FGD = 6.60E-02 lb/10^6 Btu (lb/MBtu) Filterable particulate-matter (PM_fil) emission factor for WW-fired boilers with FGD scrubber PM controls 28

AP42_SO2_emssn_factr_WW = 2.50E-02 lb/MBtu Sulfur dioxide (SO2) emission factor for WW-fired boilers with no or PM-only air-pollutn controls 28

NOx_uncontrlld_emssn_factr_WW = 2.20E-01 lb/MBtu Nitrogen oxides (NOx) emission factor for WW-fired boilers with no or PM-only air-pollutn controls 28

CO_uncontrlld_emssn_factr_WW = 6.00E-01 lb/MBtu Carbon monoxide (CO) emission factor for WW-fired boilers with no or PM-only air-pollutn controls 28

VOC_uncontrlld_emssn_factr_WW = 1.70E-02 lb/MBtu Volatile organic compds (VOC) emission factor for WW-fired boilers with no or PM-only controls 28

Trace-Element & Organic HAP Inputs:

Pb_emssn_factr_WW = 4.80E-05 lb/MBtu Lead (Pb) emission factor for WW-fired boilers with no or PM-only air-pollutn controls 28

CH2O_emssn_factr_WW = 4.40E-03 lb/MBtu Formaldehyde (CH2O) emission factor for WW-fired boilers with no or PM-only air-pollutn controls 28

PAF Unit 1 WW Criteria-Pollutant Emission Estimates:

Filterable Particulate Matter (PM_fil)

Equation (1):

WW_burn_PAF1 = WW_burn_PAF*coal_burn_PAF1/coal_burn_PAF

WW_burn_PAF1 = 0.00E+00 tpy CY05 PAF plant-total WW burn apportioned according to unit-specific share of plant-total coal burn.

Equation (2):

PM_fil_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*PM_fil_emssn_factr_WW_FGD*(ton/2000 lb)

PM_fil_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C13.

Sulfur Dioxide (SO2)

Equation (3):

SO2_uncontrlld_emssn_factr_WW = WW_S_COF/100/WW_heat_COF*(10^6 Btu/MBtu)*SO2_mol_wt/S_mol_wt

SO2_uncontrlld_emssn_factr_WW = 2.52E-01 lb/MBtu

Equation (4):

SO2_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*SO2_uncontrlld_emssn_factr_WW*(1-SO2_contrl_effncy_PAF1/100)*(ton/2000 lb)

SO2_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C17.

Nitrogen Oxides (NOx)

Equation (5):

NOx_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*NOx_uncontrlld_emssn_factr_WW*(1-NOx_contrl_effncy_PAF1/100)*(ton/2000 lb)

NOx_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C18.

Carbon Monoxide (CO)

Equation (8):

CO_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*CO_uncontrlld_emssn_factr_WW*(1-CO_contrl_effncy_PAF1/100)*(ton/2000 lb)

CO_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C19.

Volatile Organic Compounds (VOC)

Equation (9):

VOC_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*VOC_uncontrlld_emssn_factr_WW*(1-VOC_contrl_effncy_PAF1/100)*(ton/2000 lb)

VOC_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C20.

PAF Unit 1 WW Hazardous-Air-Pollutant (HAP) Emission Estimates:

Lead (Pb) Emission Estimates:

Equation (1):

Pb_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*Pb_emssn_factr_WW*(ton/2000 lb)

Pb_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C35.

CH2O Emission Estimates:

Equation (2):

CH2O_emssn_PAF1_WW = WW_burn_PAF1*(2000 lb/ton)*WW_heat_COF*(MBtu/10^6 Btu)*CH2O_emssn_factr_WW*(ton/2000 lb)

CH2O_emssn_PAF1_WW = 0.00E+00 tpy This value is listed in Table 13 of the "alt_fuel" wksheet & is included in air!C80.

Sample Calculations for PAF Unit 1 Alternate-Fuel (Used-Boiler-Cleaning Chemicals [EDTA]) Hazardous-Air-Pollutant (HAP) Emission Estimates

General Input Variables: Value Units Notes Reference

used_EDTA_burn_volume_PAF1 = 0 gallons/yr CY05 PAF Unit 1 ethylenediamine-tetraacetic-acid (EDTA) used-boiler-cleaning-chemicals total burn volume 29

No_of_rinses = 4 No. of rinses included in all CY03 TVA composite EDTA used-blr-cleaning-chemical solutions burned/evaporated 30

EDTA_burn_fraction_PAF1 = 1 Assumed composite solution for any PAF unit EDTA cleaning would be burned in PAF Unit 1 alone

Trace-Element Inputs, taking lead (Pb) as an example:

Pb_in_EDTA_composite = 2.0 milligrams per liter (mg/L) TCLP Extract analysis of worst-case composite EDTA solution from CY02 COF Unit 1 boiler cleaning 31

Pb_contrl_effncy_PAF1 = 97.96 % PAF Unit 1 coal-region weighted-avg. boiler/FGD Pb contrl effncy (cell E41 in "PAF1" wksheet)

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calcs

Lead (Pb) Emission Estimates:

Equation (1):

Pb_inputs_PAF1_EDTA = EDTA_drain_volume_PAF1*(1+No_of_rinses)*EDTA_burn_fraction_PAF1*(3.785412 L/gal)*(lb/453592.4 mg)*Pb_in_EDTA_composite*(ton/2000 lb)

Pb_inputs_PAF1_EDTA = 0.00E+00 tons/yr (tpy)

Equation (2):

Pb_emssn_PAF1_EDTA = Pb_inputs_PAF1_EDTA*(1-Pb_contrl_effncy_PAF1/100)

Pb_emssn_PAF1_EDTA = 0.00E+00 tpy This value is listed in Table 14 of the "alt_fuel" wksheet & is included in air!C35.

Sample Calculations for PAF Fugitive-Dust Emission Estimates

Potential emission estimates for coal-, limestone-, & byproduct-handling in the PAF Title V permit application (Ref. 32) were adapted to CY05 process quantities (Ref. 33) to estimate CY05 fugitive-dust emissions.

See Ref. 32 for sample calculations.

References:

(1) Excel file "CY 2005 TRI Coal Data.xls" in 2-3-06 e-mail from S.A. Godbehere to J.D. Eady et al.

(2) Excel file "CY05 Operating Statistics from DataFuser (012306).xls" in CY 05\Release Estimates\Operating Stats folder on FPG Env Affr - TRI ("chapgfs5") server.

(3) Excel file "CoalStats2005.xls" in 1-19-06 e-mail from M.A. Pendley to J.D. Lokey.

(4) Excel file "Current Particulate Test Reports Updated 02032006.xls" in 2-8-06 e-mail from W.C. Markham to J.D. Lokey.

(5) Excel file "TRI Report CY05.xls" in 2-14-06 e-mail from E.C. Miller to C.M. Anderson et al.

(6) US EPA, Compilation of Air Pollutant Emission Factors (AP-42), Vol. I, 5th Edition, Supplement E, Section 1.1, Bituminous & Subbituminous Coal Combustion, 9-98.

(7) Excel file "TVA Historic Emissions Excel 95 version.xls" in 2-15-06 e-mail from W.M. Sisk to J.D. Lokey.

(8) Median trace-element coal concentrations listed in the Electric Power Research Institute (EPRI) LARK-TRIPP (LT) Emission Estimation Model, RY2005 Version 1 (3-29-06);

 LT compilation was derived from EPRI's PISCES Database (February 2003 & 2005 updates), except mercury and chlorine (EPA ICR Part II coal database, May 2000).

(9) Chloride (Cl) concentrations reflect TVA's CY99 Information Collection Request (ICR) analyses at PAF (final compilation in 3-16-00 e-mail from J.D. Eady to R.W. Burbage).

(10) Electric Power Research Institute (EPRI), Emission Factors Handbook [EFH]--Guidelines for Estimating Trace Substance Emissions from Fossil Fuel Steam

 Electric Plants, Report No. EPRI TR-105611, November 1995, as updated in 9-98 & 2-01 EFH Addenda, 4-02 EFH Revision, & 4-05 EFH Update.

(11) Chemical Engineers' Handbook, 5th Edition, R.H. Perry & C.H. Chilton, Editors, McGraw-Hill Book Company, New York, NY, 1973.

(12) R. Hardman, R. Stacy, & E. Dismukes, "Estimating Sulfuric Acid Aerosol Emissions from Coal-Fired Power Plants," paper presented at US DOE-FETC Conference on Formation, Distribution, Impact and

 Fate of Sulfur Trioxide in Utility Flue Gas Streams, Pittsburgh, PA, March 1998; revised by K. Harrison, 7-98; by K. Harrison & L. Monroe, 9-98 (renamed "Estimating Total Sulfuric Acid Emissions from Coal-

 Fired Power Plants"); by L.S. Monroe, 5-01, and by L.S. Monroe and K.E. Harrison, 12-02 (renamed "An Updated Method for Estimating Total Sulfuric Acid Emissions from Stationary Power Plants"), and by

 K.E. Harrison, L.S. Monroe, & J.E. Cichanowicz, 10-05 (renamed "Estimating Total Sulfuric Acid Emissions from Stationary Power Plants: Revision 3 (2005)").

(13) Excel file "TRI CY05 Fossil Questionnaire.xls" dated 2-16-06, archived in the CY 05\Completed Questionnaires\PAF folder on FPG Env Affr - TRI ("chapgfs5") server.

(14) Per 3-19-03 e-mail from R.A. Babb to S.S. Koss et al., confirmed in 2-15-05 e-mail from J.D. Giles to C.M. Anderson.

(15) Per 1-11-01 conversation with R.A. Babb regarding vendor-guaranteed maximum SCR-exit NH3 slip at 20,000 hours SCR operation.

(16) Word file "PAF U2 Opacity Reduction Testing Final Report1.doc," 4-8-05, authored by M.A. Thompson, downloaded 5-25-05 from TVA Fossil Power Group (FPG) Air, Gas, Water, & Yard (AGWY) Systems'

 SO3 Mitigation website (TVA Intranet).

(17) S.L. Wilson, K.E. Harrison, & L.S. Monroe, "A Method for Estimating Total Ammonia Emissions from Stationary Power Plants," 10-05.

(18) Anhydrous & aqua ammonia receipts/usage listed in 3-13-06 e-mails from K.J. Dukes to M.F. Broder et al, archived in CY 05\Completed Questionnaires\PAF folder on FPG Env Affr - TRI ("chapgfs5") server.

(19) NH3 unloading fugitive emission factor, derived from pipe/hose dimensions at TVA's Paradise Fossil Plant (see Table 6 in "NH3" worksheet)

(20) TVA interpolation for Rocky Mtn bituminous (RMB) coal penetration & environmental factors from Ref. 17, weighted according to relative alkaline contents of RMB, PRB subbituminous, & Eastern bituminous coals.

(21) US EPA, Compilation of Air Pollutant Emission Factors (AP-42), Vol. I, 5th Edition, Supplement E, Section 1.3, Fuel Oil Combustion, 9-98.

(22) Excel file "PAFAtt1 Oper StatsReport CY 2005.xls" in 2-10-06 e-mail from M.A. Pendley to J.D. Lokey.

(23) Per 3-26-98 phone communication between D.M. Varnell & J.D. Lokey.

(24) US EPA, Compilation of Air Pollutant Emission Factors (AP-42), Vol. I, 5th Edition, Supplement B, Section 1.11, Waste Oil Combustion, 10-96

(25) Excel file "USEDOIL_FPG Reported in CY 03.xls" in 3-4-04 e-mail from M.F. Broder to J.D. Lokey et al.

(26) Excel file "Alternative Fuels TRI Data CY2005.xls," in 2-3-06 e-mail from S.A. Godbehere to R.W. Burbage et al.

(27) US EPA, Air Emissions from Scrap Tire Combustion, EPA-600/R-97-115, October 1997.

(28) US EPA, Compilation of Air Pollutant Emission Factors (AP-42), Vol. I, 5th Edition, Supplement G, Section 1.6, Wood Residue Combustion in Boilers, 3-02 [Update 2003, revised 9-03].

(29) Word file "2005 Chemicals used for Fossil Boiler Cleanings 1-13-06.doc" in CY 05\Release Estimates\Boiler Cleaning folder on FPG Env Affr - TRI ("chapgfs5") server.

(30) Per 4-5-04 email from H.G. Evans to S.S. Koss et al., all composite EDTA used-boiler-cleaning-chemical solutions burned/evaporated in CY03 consisted of first-flush EDTA drain + 4 rinses.

(31) Per 3-13-03 e-mail fr. S.S. Koss to R.W. Burbage, TCLP Extract analyses of composite (drain + rinses) EDTA solutn fr. 11-11-02 Colbert Fossil Plt (COF) Unit 1 blr cleaning were deemed "worst-case" for all TVA blr cleanings.

(32) PAF Title V permit application submitted to KY Division for Air Quality, 12-3-96.

(33) Excel file "Coal and Limestone Handled in CY 2005.xls" in 2-3-06 e-mail from S.L. Priddy to C.M. Anderson et al.

(34) US EPA, Draft "Catalog of Global Emissions Inventories and Emission Inventory Tools for Black Carbon", Jan. 2002, as cited in "Particulate Speciation Profiles for Selected Source Types" posted 3-16-06 on VISTAS website

 providing CALPUFF modeling information for BART applications (http://vistas-sesarm.org/BART/calpuff.asp) & in National Park Service (NPS) website (http://www2.nature.nps.gov/air/permits/ect/ectCoalFiredBoiler.cfm)

(35) Excel file "2006FinalCycloneFurnaceESPpmSpeciationProfile.xls" posted on National Park Service (NPS) website (http://www2.nature.nps.gov/air/permits/ect/ectCoalFiredBoiler.cfm).

TVA Environmental Technologies

07/12/06

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